U.S. patent number 7,670,837 [Application Number 11/304,589] was granted by the patent office on 2010-03-02 for non-tumorigenic mdck cell line for propagating viruses.
This patent grant is currently assigned to Medimmune, LLC. Invention is credited to John Michael Berry, Richard Schwartz, Xiao Shi, Ajit Subramanian.
United States Patent |
7,670,837 |
Schwartz , et al. |
March 2, 2010 |
Non-tumorigenic MDCK cell line for propagating viruses
Abstract
The present invention provides novel MDCK-derived adherent
non-tumorigenic cell lines that can be grown in the presence or
absence of serum. The cell lines of the present invention are
useful for the production of vaccine material (e.g., viruses). More
specifically, the cell lines of the present invention are useful
for the production of influenza viruses in general and ca/ts
influenza viruses in particular. The invention further provides
methods and media formulations for the adaptation and cultivation
of MDCK cells such that they remain non-tumorigenic. Additionally,
the present invention provides methods for the production of
vaccine material (e.g., influenza virus) in the novel cell lines of
the invention.
Inventors: |
Schwartz; Richard (San Mateo,
CA), Berry; John Michael (Belmont, CA), Subramanian;
Ajit (Berkeley, CA), Shi; Xiao (Cupertino, CA) |
Assignee: |
Medimmune, LLC (Gaithersburg,
MD)
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Family
ID: |
36615395 |
Appl.
No.: |
11/304,589 |
Filed: |
December 16, 2005 |
Prior Publication Data
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Document
Identifier |
Publication Date |
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US 20060188977 A1 |
Aug 24, 2006 |
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Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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60638166 |
Dec 23, 2004 |
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60641139 |
Jan 5, 2005 |
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Current U.S.
Class: |
435/350; 435/377;
435/375; 435/325; 435/237 |
Current CPC
Class: |
C12N
7/00 (20130101); A61P 37/04 (20180101); C12N
5/0037 (20130101); A61P 31/12 (20180101); C12N
5/0043 (20130101); A61P 31/16 (20180101); C12N
2501/11 (20130101); C12N 2760/16161 (20130101); C12N
2510/02 (20130101); C12N 2760/16261 (20130101); C12N
2760/16251 (20130101); C12N 2501/395 (20130101); C12N
2500/76 (20130101); C12N 2500/36 (20130101); C12N
2500/90 (20130101); C12N 2760/16151 (20130101) |
Current International
Class: |
C12N
5/00 (20060101); C12N 5/02 (20060101); C12N
7/08 (20060101); C12N 5/16 (20060101) |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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0891420 |
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Feb 2005 |
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EP |
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1739167 |
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Jan 2007 |
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EP |
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1862537 |
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Dec 2007 |
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EP |
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WO-2004-110484 |
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Dec 2004 |
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WO |
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WO-2005-026333 |
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Mar 2005 |
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WO |
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WO-2005-113758 |
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Dec 2005 |
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WO |
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WO-2006-071563 |
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Dec 2006 |
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WO |
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Primary Examiner: Chen; Stacy B
Assistant Examiner: Blumel; Benjamin P
Parent Case Text
CROSS REFERENCE TO RELATED APPLICATIONS
This application claims the benefit under 35 U.S.C. .sctn.119(e) of
the following U.S. Provisional Application Nos.: 60/638,166 filed
Dec. 23, 2004 and 60/641,139 filed Jan. 5, 2005. The priority
applications are hereby incorporated by reference herein in their
entirety for all purposes.
Claims
The invention claimed is:
1. A cell culture composition comprising non-tumorigenic MDCK
cells, wherein said non-tumorigenic MDCK cells are of the MDCK-SF
103 cell line deposited as ATCC Accession Number PTA-6503.
2. A non-tumorigenic MDCK cell line selected from the group
consisting of: MDCK-S deposited as ATCC Accession Number PTA-6500;
and MDCK-SF 103 deposited as ATCC Accession Number PTA-6503.
3. The cell culture composition of claim 1, wherein said
non-tumorigenic MDCK cells are non-tumorigenic in an adult nude
mouse model.
4. The cell culture composition of claim 1, wherein said
non-tumorigenic MDCK cells remain non-tumorigenic after at least 20
passages.
5. The non- tumorigenic MDCK cell line of claim 2, wherein said
cell line is MDCK-S deposited as ATCC Accession Number
PTA-6500.
6. The non- tumorigenic MDCK cell line of claim 2, wherein said
cell line is MDCK-SF 103 deposited as ATCC Accession Number
PTA-6503.
7. The non- tumorigenic MDCK cell line of claim 2, wherein said
cell line is non-tumorigenic in an adult nude mouse model.
8. The non- tumorigenic MDCK cell line of claim 2, wherein said
cell line remains non-tumorigenic after at least 20 passages.
Description
FIELD OF THE INVENTION
The present invention relates to novel non-tumorigenic MDCK cells,
which can be used for the production of vaccine material. The
non-tumorigenic MDCK cells may be adapted to serum-free culture
medium. The present invention further relates to media formulations
and cultivation methods for the propagation of the non-tumorigenic
MDCK cells as well as methods for maintaining the non-tumorigenic
nature of the cell lines of the invention. The present invention
further relates to processes for the production of influenza
viruses in cell culture using non-tumorigenic MDCK cells. The
present invention also relates to the viruses (e.g., influenza)
obtainable by the process described and immunogenic compositions
which contain viruses of this type and/or components thereof.
BACKGROUND OF THE INVENTION
Vaccination is the most important public health measure for
preventing disease caused by annual epidemics of influenza. The
effective use of vaccines is dependent on being able to quickly
produce large quantities of vaccine material (e.g., virus) from a
stable and easy to cultivate source. The rapid development of
vaccines and their abundant availability is critical in combating
many human and animal diseases. Delays in producing vaccines and
shortfalls in their quantity can cause problems in addressing
outbreaks of disease. For example, recent studies suggest that
there is cause for concern regarding the long lead times required
to produce vaccines against pandemic influenza. See, for example,
Wood, J. M., 2001, Philos. Trans. R. Soc. Lond. B. Biol. Sci.,
356:1953. Efficient vaccine production requires the growth of large
quantities of vaccine material produced in high yields from a host
system. Different vaccine materials require different growth
conditions in order to obtain acceptable yields. Vaccine material
may be produced in embryonated eggs, primary tissue culture cells,
or in established cell lines. However, these host systems currently
suffer from a number of limitations detailed below.
Embryonated eggs are typically used for influenza vaccine virus
production in a time-, labor-, and cost intensive process that
necessitates the management of chicken breeding and egg
fertilization. In addition, influenza vaccine produced in eggs is
contraindicated for persons with egg allergies due to the severe
immediate hypersensitivity reaction that can occur. Thus, there has
been an effort by the vaccine industry to develop alternative
production platforms that do not utilize eggs such as producing
influenza vaccine in a cell culture system.
The use of primary tissue culture cells is hampered by the
difficulties encountered in developing and maintaining a stable
primary cell population. Often established cells lines are used to
circumvent the technical limitations of primary cells. However,
many of these cell lines are known to be tumorigenic and as such
raise safety concerns and are subject to significant regulatory
constraints against their use for vaccine production. In fact, the
applicable guidelines of the World Health Organization indicate
that only a few cell lines are allowed for vaccine production.
Additional problems arise from the use of serum and/or protein
additives derived from animal or human sources in cell culture
media. For example, variability in the quality and composition
among lots of additives and the risk of contamination with
mycoplasma, viruses, BSE-agents and other infectious agents are
well known. In general, serum or serum-derived substances like
albumin, transferrin or insulin may contain unwanted agents that
can contaminate the culture and the biological products produced
from therefrom. Therefore, many groups are working to develop
efficient host systems and cultivation conditions that do not
require serum or serum derived products.
Consequently, there has been a demand for establishing a
non-tumorigenic cell line useful for the production of vaccine
materials in a low-cost, highly safe and stable manner preferably
in serum-free or in animal protein-free culture conditions. Such a
cell system would be particularly useful for the production of
influenza vaccine material.
Madin Darby Canine Kidney (MDCK) cells have been traditionally used
for the titration of influenza viruses (Zambon M., in Textbook of
Influenza, ed Nicholson, Webster and Hay, pg 291-313, Blackwell
Science (1998)). These cells were established in 1958 from the
kidney of a normal male cocker spaniel. The ATCC list the MDCK (CCL
34) line as having been deposited by S. Madin and N. B. Darby
however, numerous other lineages of MDCK cells are available.
Leighton J and his coworkers published a series of papers (Leighton
et al.,1969, Science 163:472; Leighton et al., 1970, Cancer 26:1022
and Leighton et al., 1972 Europ J. Cancer 8:281) documenting the
oncogenic characteristics of the MDCK cells. However, the lineage
and passage number of the MDCK cells used for these studies was not
described and it was already known that MDCK cells from different
lineages and different passages showed changes in chromosome
numbers and structure (Gaush et al., 1966, Proc. Soc. Exp. Biol.
Med., 122: 931) which could result in cells with tumorigenic
properties.
Since one of the major considerations for the acceptability of a
cell line for vaccine production concerns the potential malignancy
of those cells the use of MDCK cells for the production of vaccine
material using currently described cell lines is limited. Groner et
al. (U.S. Pat. No. 6,656,720) and Makizumi et al. (U.S. Pat. No.
6,825,036) both purport to disclose cell lines derived from MDCK
cells which have been adapted to grow in serum-free media in
suspension and which can be utilized for the production of
influenza virus. However, it has been reported that there is
correlation between the loss of anchorage requirement and the
transformation of normal animal cells to cells which are
tumorigenic (Stiles et al., 1976, Cancer Res., 36:3300). Several
groups (Kessler et al., 1999, Cell Culture Dev Biol Stand, 98:13;
Merten et al., 1999, Cell Culture Dev Biol Stand, 98:23 and Tree et
al., 2001, Vaccine, 19:3444) purport to describe the use of MDCK
cells for the large-scale production of influenza virus; however,
they do not address the potential transformation of the MDCK cells
used.
Citation or discussion of a reference herein shall not be construed
as an admission that such is prior art to the present invention. In
addition, citation of a patent shall not be construed as an
admission of its validity.
SUMMARY OF THE INVENTION
The present invention provides non-tumorigenic MDCK cells which
have been adapted to grow in either serum containing or serum-free
media formulations including animal protein-free (APF)
formulations. In one embodiment, the non-tumorigenic MDCK cells of
the invention are adherent. In another embodiment, the
non-tumorigenic MDCK cells of the invention have an epithelial
morphology. In yet another embodiment, the non-tumorigenic MDCK
cells of the invention are adherent and have an epithelial
morphology. Tumorigenicity is in one embodiment, determined by the
adult nude mouse model (e.g., Stiles et al., 1976, Cancer Res,
36:1353, and Example 2 below). Tumorigenicity may also be tested by
other assays, for example, by injection into a chick embryo and/or
topical application to the chorioallantois (Leighton et al., 1970,
Cancer, 26:1022).
Viruses that can be grown in the MDCK cells of the invention
include but are not limited to negative strand RNA viruses,
including but not limited to influenza, RSV, parainfluenza viruses
1, 2 and 3, and human metapneumovirus.
The present invention further provides methods and media
formulations useful for the derivation and maintenance of
non-tumorigenic MDCK cells. The MDCK cells of the invention are
particularly useful for the production of vaccine material such as,
for example, viruses.
Other aspects of the invention include methods of producing vaccine
material (e.g., virus) by culturing any MDCK cell of the invention,
in a suitable culture medium under conditions permitting production
of vaccine material and, isolating the material from one or more of
the host cell or the medium in which it is grown.
Immunogenic compositions are also features of the invention. For
example, immunogenic compositions comprising the vaccine material
produced as described above and, optionally, an excipient such as a
pharmaceutically acceptable excipient or one or more
pharmaceutically acceptable administration component.
Methods of producing immunogenic responses in a subject through
administration of an effective amount of one or more above
described immunogenic compositions to a subject are also within the
current invention. Additionally, methods of prophylactic or
therapeutic treatment of a viral infection (e.g., viral influenza)
in a subject through administration of one or more above described
immunogenic compositions in an amount effective to produce an
immunogenic response against the viral infection are also part of
the current invention. Subjects for such treatment can include
mammals (e.g., humans). Additionally, such methods can also
comprise administration of a composition of one or more viruses
produced in the MDCK cells of the invention and a pharmaceutically
acceptable excipient that is administered to the subject in an
amount effect to prophylactically or therapeutically treat the
viral infection.
These and other objects and features of the invention will become
more fully apparent when the following detailed description is read
in conjunction with the accompanying figures appendix.
BRIEF DESCRIPTION OF THE FIGURES
FIG. 1 Growth of Influenza strains in cells. Panel A is a
photograph showing the results of a fluorescent focus assay
comparing the spread of infection of a representative ca/ts
influenza strain in MDCK cells and a Vero Cell Clone (27F9). Panel
B is a growth curve of influenza strain ca A/Vietnam/1203/2004
(H5N1) in MDCK cells. Titers peaked at 48 hours post infection at
.about.8 log.sub.10 TCID.sub.50/mL and remained stable for the next
3 to 4 days.
FIG. 2 outlines the process used for the derivation of MDCK-S
PreMCB (passage No. 57). The process is described in detail in
Example 2.
FIG. 3 is a photograph showing that MDCK-S cells have an
epithelial-like morphology. The photo was taken 3 days after
seeding.
FIG. 4 is the growth curve of MDCK-S cells in 10% FBS DMEM medium.
Cells had about a 1 day lag phase followed by exponential growth
entering stationary phase at day 4 post seeding achieving a maximum
density of .about.29.times.10.sup.6 cells on day 5.
FIG. 5 is a graph of the glucose consumption and lactate production
of MDCK-S cells in 10% FBS DMEM medium. The rates were low during
lag phase increasing to 2.93 mM/day and 3.43 mM/day for glucose and
lactate, respectively.
FIG. 6 is a graph of the glutamine consumption and both glutamate
and ammonia production of MDCK-S cells in 10% FBS DMEM medium. The
glutamine consumption rate was 0.49 mM/day up to day 4 and the
ammonia production rate was 0.32 mM/day up to day 5. Glutamate did
not accumulate in this study.
FIG. 7 is a plot of the distributions of chromosome number in 100
metaphase low passage (P61/4) and high passage (P81/24) MDCK-S
cells. The chromosome count ranged from 70 to 84 per metaphase with
a modal chromosome number of 78 for both the high and low passage
cells.
FIG. 8 outlines the process used for the derivation of MDCK-T
PreMCB (passage No. 64/5). The process is described in detail in
Example 3.
FIG. 9 is a photograph showing that MDCK-T cells have an
epithelial-like morphology. The photo was taken 3 days after
seeding.
FIG. 10 is the growth curve of MDCK-T cells in Taub's media. Cells
had no lag phase and were in exponential growth until entering
stationary phase at day 4 post seeding.
FIG. 11 is a graph of the glucose consumption and lactate
production of MDCK-T cells in Taub's media. During the exponential
phase the rates were 1.78 mM/day and 2.88 mM/day for glucose and
lactate, respectively.
FIG. 12 is a graph of the glutamine consumption and both glutamate
ammonia production of MDCK-T cells in Taub's media. The glutamine
consumption rate was 0.36 mM/day up to day 4 and the ammonia
production rate increased linearly up to day 7 at a rate of 0.22
mM/day. Glutamate did not accumulate in this study.
FIG. 13 is a plot of the distributions of chromosome number in 100
metaphase low passage (P61/4) and high passage (P81/24) MDCK-T
cells. The chromosome count ranged from 52 to 82 per metaphase for
low passage cells and from 54 to 82 for high passage cells.
FIG. 14 is a plot of the distributions of chromosome number in 100
metaphase MDCK-T, MDCK-SF101 (passage 71/9) and MDCK-SF102 cells
(passage 71/9). Both SF101 and SF102 cells had a modal chromosome
number of 78, with the chromosome count ranging from 70 to 82 and
60 to 80 per metaphase for SF101 and SF102, respectively.
FIG. 15 is a photograph showing that MDCK-SF103 have an have an
epithelial-like cell morphology. The photo was taken 3 days after
seeding.
FIG. 16 is the growth curve of MDCK-SF103 cells in MediV SFM103.
Cells had about a 1 day lag phase followed by exponential growth
entering stationary phase at day 4 post seeding achieving a maximum
density of .about.17.times.10.sup.6 cells on day 4.
FIG. 17 is a graph of the glucose consumption and lactate
production of MDCK-SF103 cells in MediV SFM103. During the
exponential phase the glucose consumption and lactate production
mirrored each other with lactate increasing in concentration as the
glucose concentration decreased
FIG. 18 is a graph of the glutamine consumption and both ammonia
and glutamate production of MDCK-SF103 cells in MediV SFM103. The
ammonia production rate increased nearly linearly up to day 7.
Glutamate did not accumulate in this study.
FIG. 19 is a plot of the distributions of chromosome number in 100
metaphase MDCK-SF103 cells at passage 87. SF103 cells had a modal
chromosome number of 78, with the chromosome count ranging from 66
to 80.
FIG. 20 Production Scale Growth and Purifiction. Panel A is a plot
of the yield obtained for several vaccine reassortant strains,
B/Victoria/504/2000 (.about.8 LogTCID 50/mL), A/Sydney/05/97
(.about.7.85 LogTCID 50/mL) and A/New Calcdonia/20/99 (.about.8.2
LogTCID 50/mL), from 250 mL spinner flasks of MDCK-SF103 grown on
Cytodex beads. Panel B outlines one cell culture scale up process
which can be utilized for commercial scale production of vaccine
material.
DETAILED DESCRIPTION OF THE INVENTION
The present invention is based in part on the discovery that MDCK
cells can be cultivated under conditions wherein they remain
non-tumorigenic. The present invention provides non-tumorigenic
cell lines, including MDCK cell lines and other types of cells
which have been adapted to a variety of cell culture conditions
including serum-free media formulations and are referred to herein
as "cells of the invention". In addition, the present invention
provides cell culture compositions comprising cells of the
invention and other components including, but not limited to, media
(e.g., a media disclosed herein), media components, buffers,
chemical compounds, additional cell types, viral material (e.g.,
viral genomes, viral particles) and heterologous proteins. The
present invention also provides methods and media formulations
useful for the cultivation of non-tumorigenic cells, including MDCK
cells, with one more specific characteristics including but not
limited to, being non-tumorigenic (e.g., not forming nodules in a
nude mouse) and/or growth as adherent cells and/or having an
epithelial-like morphology and/or supporting the replication of
various viruses including but not limited to orthomyxoviruses,
paramyxoviruses, rhabdoviruses and flavoviruses. The culture
conditions of the present invention include serum containing and
serum-free media formulations, as well as animal protein-free (APF)
formulations. In addition, the present invention also provides
methods of producing vaccine material (e.g., influenza virus) in
non-tumorigenic cells, including MDCK cells, preparing vaccine
material from non-tumorigenic cells, and methods of preventing
influenza infection utilizing vaccine materials produced in
non-tumorigenic cells. The cells of the invention are particularly
useful for the production of cold adapted/temperature
sensitive/attenuated (ca/ts/att) influenza strains (e.g., those in
FluMist.RTM.) which do not replicate as efficiently in other
mammalian cell lines (e.g., Vero, PerC6, HEK-293, MRC-5 and WI-38
cells).
Cell Characteristics
The cells according to the invention are in one embodiment,
vertebrate cells. In another embodiment, the cells of the invention
are mammalian cells, e.g., from hamsters, cattle, monkeys or dogs,
in particular kidney cells or cell lines derived from these. In
still another embodiment, the cells of the invention are MDCK cells
(e.g., derived from ATCC CCL-34 MDCK) and are specifically referred
to herein as "MDCK cells of the invention" and are encompassed by
the term "cells of the invention". In a specific embodiment, the
cells of the invention are derived from ATCC CCL-34 MDCK. Cells of
the invention may be derived from CCL-34 MDCK cells by methods well
known in the art. For example, the CCL-34 MDCK cells may be first
passaged a limited number of times in a serum containing media
(e.g., Dulbecco's Modified Eagle Medium (DMEM)+10% Fetal Bovine
Serum (FBS)+4 mM glutamine+4.5 g/L glucose, or other media
described herein) followed by cloning of individual cells and
characterization of the clones. Clones with superior biological and
physiological properties including, but not limited to, doubling
times, tumorigenicity profile and viral production, are selected
for the generation of a master cell bank (MCB). In one aspect, the
cells of the invention are adapted to growth in a media of choice
(e.g., a serum-free or APF media, such as those described herein).
Such adaptation may occur prior to, concurrently with, or
subsequent to the cloning of individual cells. In certain
embodiments, cells of the invention are adapted to grow in MediV
SF101, MediV SF102, MediV SF103, MediV SF104 or MediV SF105. Cells
of the invention adapted to grow in these media are referred to
herein as "MDCK-SF101, MDCK-SF102, MDCK-SF103, MDCK-SF104 and
MDCK-SF105" cells, respectively and as "MDCK-SF cells"
collectively. In other embodiments, cells of the invention are
adapted to grow in serum containing media (e.g., Dulbecco's
Modified Eagle Medium (DMEM)+10% Fetal Bovine Serum (FBS)+4 mM
glutamine+4.5 g/L glucose), such cells are referred to herein as
"MDCK-S" cells. MDCK-SF and MDCK-S cells are also encompassed by
the terms "cells of the invention" and "MDCK cells of the
invention".
In a specific embodiment of the invention the cells are of the cell
lines including, but not limited to, those which have been
deposited with the American Type Culture Collection (10801
University Boulevard, Manassas, Va. 20110-2209) and assigned ATCC
Deposit Nos. PTA-6500 (Deposited on Jan. 5, 2005), PTA-6501
(Deposited on Jan. 5, 2005), PTA-6502 (Deposited on Jan. 5, 2005),
and PTA-6503 (Deposited on Jan. 5, 2005), these cells are referred
to herein as "MDCK-S, MDCK-SF101, MDCK-SF102 and MDCK-SF103",
respectively and as "the MDCK cells of the invention" collectively.
These deposits will be maintained under the terms of the Budapest
Treaty on the International Recognition of the Deposit of
Microorganisms for the Purposes of Patent Procedure. In one
embodiment, the MDCK cells of the invention are used to generate a
cell bank useful for the preparation of vaccine material suitable
for approval by the U.S. Food and Drug Administration for human
use.
The cells lines MDCK-S, MDCK-SF101, MDCK-SF102, MDCK-SF103,
MDCK-SF104 and MDCK-SF105 are derived from the cell line MDCK (CCL
34) by passaging and selection with respect to one or more specific
characteristics including but not limited to, growing as adherent
cells either in serum containing, or serum-free media or animal
protein-free media, having an epithelial-like morphology, being
non-tumorigenic (e.g., not forming nodules in a nude mouse) and/or
supporting the replication of various viruses including but not
limited to orthomyxoviruses, paramyxoviruses, rhabdoviruses and
flavoviruses.
In one embodiment, the MDCK cells of the invention are
non-tumorigenic. Methods for determining if cells are tumorigenic
are well known in the art (see, for example, Leighton et al., 1970,
Cancer, 26:1022 and Stiles et al., 1976, Cancer Res, 36:1353), the
method currently preferred by the U.S. Food and Drug Administration
using the nude mouse model is detailed in Example 2 below. In a
specific embodiment, the MDCK cells of the invention are
non-tumorigenic in the adult nude mouse model (see, Stiles et al.,
Id and Example 2 below). In another specific embodiment, the MDCK
cells of the invention are non-tumorigenic when injected into a
chick embryo and/or topically applied to the chorioallantois (see,
Leighton et al., Id). In still another embodiment, the MDCK cells
of the invention are non-tumorigenic in the adult nude mouse model
but not when injected into a chick embryo and/or topically applied
to the chorioallantois. In yet another embodiment, the MDCK cells
of the invention are non-tumorigenic in the adult nude mouse model
and when injected into a chick embryo and/or topically applied to
the chorioallantois. In still another embodiment, the MDCK(cells of
the invention are non-tumorigenic after at least 20 passages, or
after at least 30 passages, or after at least 40 passages, or after
at least 50 passages, or after at least 60 passages, or after at
least 70 passages, or after at least 80 passages, or after at least
90 passages, or after at least 100 passages in a medium. In yet
another specific embodiment the medium is a media described herein
(e.g., Medi SF103).
Tumorigenicity may be quantified in numerous ways known to one of
skill in the art. One method commonly utilized is to determine the
"TD.sub.50" value which is defined as the number of cells required
to induce tumors in 50% of the animals tested (see, e.g., Hill R.
The TD.sub.50 assay for tumor cells. In: Potten C, Hendry J,
editors. Cell clones. London: Churchill Livingstone; 1985. p. 223).
In one embodiment, the MDCK cells of the invention have a TD.sub.50
value of between about 10.sup.10 to about 10.sup.1, or between
about 10.sup.8 to about 10.sup.3, or between about 10.sup.7 to
about 10.sup.4. In a specific embodiment, the MDCK cells of the
invention have a TD.sub.50 value of more than about 10.sup.10, or
of more than about 10.sup.9, or of more than about 10.sup.8, or of
more than about 10.sup.7, or of more than about 10.sup.6, or of
more than about 10.sup.5, or of more than about 10.sup.4, or of
more than about 10.sup.3, or of more than about 10.sup.2, or of
more than about 10.sup.1.
In another embodiment, the non-tumorigenic cells of the invention
grow as adherent cells either in serum containing or serum-free
media or animal protein-free media. In still another embodiment,
the non-tumorigenic cells of the invention have an epithelial-like
morphology. In yet another embodiment, the MDCK cells of the
invention support the replication of various viruses including but
not limited to orthomyxoviruses, paramyxoviruses, rhabdoviruses and
flavoviruses. It is contemplated that the MDCK cells of the
invention may have any combination of one or more specific
characteristics including but not limited to, being
non-tumorigenic, growing as adherent cells, having an
epithelial-like morphology and supporting the replication of
various viruses.
It is contemplated that each and every passage of the MDCK cells of
the invention is documented in sufficient detail such that the
complete lineage of each cell line is available. The documentation
of each and every passage may facilitate approval by the U.S. Food
and Drug Administration and other regulatory bodies around the
world for the use of the MDCK cells of the invention for the
preparation of vaccine material.
In another embodiment, the MDCK cells of the invention are free of
microbial contaminants (e.g., bacterial, viral and fungal
contaminants). Methods for testing for the presence of bacterial
and fungal contaminants are well known in the art and routinely
performed by commercial contractors (e.g., BioReliance.RTM.,
Rockville, Md.). Accepted microbial sterility and mycoplasm tests
are detailed in Example 2 below. Specific examples of microbial
agents which may be tested for are listed in Table 6.
In yet another embodiment, the MDCK cells of the invention support
the replication of viruses including but not limited to
orthomyxoviruses (including influenza A and/or B strains),
paramyxoviruses (including RSV A and/or B, human metapneumovirus
and parainfluenza 1, 2 and/or 3), rhabdoviruses and flavoviruses.
In a specific embodiment, the MDCK cells of the invention support
the replication of cold adapted/temperature sensitive (ca/ts)
influenza viruses such as those found, for example, in FluMist.RTM.
(Belshe et al., 1998, N Engl J Med 338:1405; Nichol et al., 1999,
JAMA 282:137; Jackson et al., 1999, Vaccine, 17:1905) and/or
reassortant viruses comprising the backbone of these viruses or
comprising the backbone (or one or more vRNA segment(s)) of
influenza viruses having one or more of the following
characteristics: cold adapted, attenuated, and temperature
sensitive. One indication of the ability of a cell to support viral
replication is the yield of virus obtained from an infected cell
culture. Viral yield can be determined by numerous methods known to
one skilled in the art. For example, viral yield can be quantified
by determining the concentration of virus present in a sample
according to a median tissue culture infectious dose (TCID.sub.50)
assay that measures infectious virions. The TCID.sub.50 values are
often reported as the log.sub.10 TCID.sub.50/mL. In one embodiment,
the MDCK cells of the invention support the replication of
influenza viruses (e.g., ca/ts strains) to a log.sub.10
TCID.sub.50/mL of at least 6.0, or at least 6.2, or at least 6.4,
or at least 6.6, or at least 6.8, or at least 7.0, or at least 7.2,
or at least 7.4, or at least 7.6, or at least 7.8, or at least 8.0,
or at least 8.2, or at least 8.4, or at least 8.6, or at least 8.8,
or at least 9.0, or at least 9.2, or at least 9.4, or at least 9.6,
or at least 9.8. In another embodiment, the MDCK cells of the
invention support the replication of influenza viruses (e.g., ca/ts
strains) to a log.sub.10 TCID.sub.50/mL of at least about 6.0, or
at least about 6.2, or at least about 6.4, or at least about 6.6,
or at least about 6.8, or at least about 7.0, or at least about
7.2, or at least about 7.4, or at least about 7.6, or at least
about 7.8, or at least about 8.0, or at least about 8.2, or at
least about 8.4, or at least about 8.6, or at least about 8.8, or
at least about 9.0, or at least about 9.2, or at least about 9.4,
or at least about 9.6, or at least about 9.8.
It will be understood by one of skill in the art that the cells of
the invention will generally be part of a cell culture composition.
The components of a cell culture composition will vary according to
the cells and intended use. For example, for cultivation purposes a
cell culture composition may comprise cells of the invention and a
suitable media for growth of the cells. Accordingly, the present
invention provides cell culture compositions comprising cells of
the invention and other components including, but not limited to,
media (e.g., a media disclosed herein), media components, buffers,
chemical compounds, additional cell types, viral material (e.g.,
viral genomes, viral particles) and heterologous proteins. In one
embodiment, a cell culture composition comprises cells of the
invention and a media or components thereof. Media which may be
present in a cell culture composition include serum-free media,
serum containing media and APF media. In one embodiment, a cell
composition comprises a media disclosed herein (e.g., MediV SF101,
MediV SF102, MediV SF103, MediV SF104 or MediV SF105) or components
thereof.
Methods and Media Formulations
The present invention provides methods and media formulations for
the cultivation of non-tumorigenic MDCK cells in serum containing
media. The present invention also provides methods for the
adaptation to and subsequent cultivation of non-tumorigenic MDCK
cells in serum-free media including APF media formulations. In
certain aspects of the invention, the medias are formulated such
that the MDCK cells retain one or more of the following
characteristics including but limited to, being non-tumorigenic,
growing as adherent cells, having an epithelial-like morphology and
supporting the replication of various viruses when cultured. It is
contemplated that the media formulations disclosed herein or
components thereof, may be present in a cell culture
compostion.
Serum containing media formulations are well known in the art.
Serum containing media formulations include but are not limited to,
Dulbecco's Modified Eagle Medium (DMEM)+Fetal Bovine Serum
(FBS)+glutamine+glucose. In one embodiment, FBS is present in a
serum containing media at a concentration between about 1% and
about 20%, or between about 5% and about 15%, or between about 5%
and about 10%. In a specific embodiment, FBS is present in a serum
containing media at a concentration of 10%. In another embodiment,
glutamine is present in a serum containing media at a concentration
of between about 0.5 mM and about 10 mM, or between about 1 mM and
10 mM, or between about 2 mM and 5 mM. In a specific embodiment,
glutamine is present in a serum containing media at a concentration
of 4 mM. In still another embodiment, glucose is present in a serum
containing media at a concentration of between about 1 g/L and
about 10 g/L, or between about 2 g/L and about 5 g/L. In a specific
embodiment, glucose is present in a serum containing media at a
concentration of 4.5 g/L. In yet another embodiment, a serum
containing media formulation comprises, FBS at a concentration
between about 1% and about 20%, glutamine at a concentration of
between about 0.5 mM and about 10 mM, and glucose a concentration
of between about 1 g/L and about 10 g/L. In a specific embodiment,
a serum containing media formulation comprises, Dulbecco's Modified
Eagle Medium (DMEM)+10% Fetal Bovine Serum (FBS)+4 mM glutamine+4.5
g/L glucose. DMEM is readily available from numerous commercial
sources including, for example, Gibco/BRL (Cat. No. 11965-084). FBS
is readily available from numerous commercial sources including,
for example, JRH Biosciences (Cat. No. 12107-500M). While FBS is
the most commonly applied supplement in animal cell culture media,
other serum sources are also routinely used and encompassed by the
present invention, including newborn calf, horse and human.
In one embodiment, MDCK-S serum adapted non-tumorigenic cells of
the invention are derived from Madin Darby Canine Kidney Cells
(MDCK) cells obtained from the American type Culture Collection
(ATCC CCL34) by culturing them in a chemically defined media
supplemented with serum. In a specific embodiment, MDCK cells (ATCC
CCL34) are expanded in a chemically defined media supplemented with
serum to generate the MDCK-S cell line as follows: The MDCK (ATCC
CCL34) cells are passaged as need in Dulbecco's Modified Eagle
Medium (DMEM) supplemented with fetal bovine serum (10% v/v), 4 mM
glutamine and 4.5 g/L glucose to obtain enough cell to prepare a
frozen pre Master Cell Bank (PreMCB) designated MDCK-S. In another
specific embodiment, the cells are cultured using the process
detailed in Example 2, infra. It is specifically contemplated that
the MDCK-S serum adapted cell are passaged for another 20 passages
or more, from a vial of PreMCB and tested for tumorigenicity in an
vivo adult nude mice model and karyology in a karyotype assay. In
certain embodiments, the expanded MDCK-S cells will not produce
nodules when injected subcutaneously into adult nude mice and will
have a modal chromosome number of 78 with a range of chromosome
numbers of no more then about 60-88, or of no more then about
65-85, or of no more than about 65-80, or of no more then about
70-85. In one embodiment, the MDCK-S cells are non-tumorigenic
after at least 20 passages, or after at least 30 passages, or after
at least 40 passages, or after at least 50 passages, or after at
least 60 passages, or after at least 70 passages, or after at least
80 passages, or after at least 90 passages, or after at least 100
passages in a medium (e.g., a media described herein).
It will be appreciated by one of skill in the art that the use of
serum or animal extracts in tissue culture applications may have
drawbacks (Lambert, K. J. et al., In: Animal Cell Biotechnology,
Vol 1, Spier, R. E. et al., Eds., Academic Pres New York, pp.
85-122 (1985)). For example, the chemical composition of these
supplements may vary between lots, even from a single manufacturer.
In addition, supplements of animal or human origin may also be
contaminated with adventitious agents (e.g., mycoplasma, viruses,
and prions). These agents can seriously undermine the health of the
cultured cells when these contaminated supplements are used in cell
culture media formulations. Further, these agents may pose a health
risk when substances produced in cultures contaminated with
adventitious agents are used in cell therapy and other clinical
applications. A major fear is the presence of prions which cause
spongiform encephalopathies in animals and Creutzfeld-Jakob disease
in humans. Accordingly, the present invention further provides
serum-free media formulations.
Serum-free media formulations of the invention include but are not
limited to MediV SF101 (Taub's+Plant Hydrolysate), MediV SF102
(Taub's+Lipids), MediV SF103 (Taub's+Lipds+Plant Hydrolysate),
MediV SF104 (Taub's+Lipds+Plant Hydrolysate+growth factor) and Medi
SF105 (same as MediV SF104 except transferrin is replaced with
Ferric ammonium citrate/Tropolone or Ferric ammonium
sulfate/Tropolone). It is specifically contemplated that Taub's SF
medium (Taub and Livingston, 1981, Ann NY Acad. Sci., 372:406) is a
50:50 mixture of DMEM and Ham's F12 supplemented with hormones, 5
.mu.g/mL insulin, 5 .mu.g/mL transferrin, 25 ng/mL prostaglandin
E1, 50 nM hydrocortisone, 5 pM triidothyronine and 10 nM
Na.sub.2SeO.sub.3, 4.5 g/L glucose, 2.2 g/L NaHCO.sub.3 and 4 mM
L-glutamine. Taub's SF medium is also referred to herein as Taub's
medium or simply "Taub's".
Plant hydrolysates include but are not limited to, hydrolysates
from one or more of the following: corn, cottonseed, pea, soy,
malt, potato and wheat. Plant hydrolysates may be produced by
enzymatic hydrolysis and generally contain a mix of peptides, free
amino acids and growth factors. Plant hydrolysates are readily
obtained from a number of commercial sources including, for
example, Marcor Development, HyClone and Organo Technie. It is also
contemplated that yeast hydrolysates my also be utilized instead
of, or in combination with plant hydrolysates. Yeast hydrolysates
are readily obtained from a number of commercial sources including,
for example, Sigma-Aldrich, USB Corp, Gibco/BRL and others.
Lipids that may be used to supplement culture media include but are
not limited to chemically defined animal and plant derived lipid
supplements as well as synthetically derived lipids. Lipids which
may be present in a lipid supplement includes but is not limited
to, cholesterol, saturated and/or unsaturated fatty acids (e.g.,
arachidonic, linoleic, linolenic, myristic, oleic, palmitic and
stearic acids). Cholesterol may be present at concentrations
between 0.10 mg/ml and 0.40 mg/ml in a 100.times. stock of lipid
supplement. Fatty acids may be present in concentrations between 1
.mu.g/ml and 20 .mu.g/ml in a 100.times. stock of lipid supplement.
Lipids suitable for media formulations are readily obtained from a
number of commercial sources including, for example HyClone,
Gibco/BRL and Sigma-Aldrich.
In one embodiment, Taub's media is supplemented with a plant
hydrolysate and a final concentration of at least 0.5 g/L, or at
least 1.0 g/L, or at least 1.5 g/L, or at least 2.0 g/L, or at
least 2.5 g/L, or at least 3.0 g/L, or at least 5.0 g/L, or at
least 10 g/L, or at least 20 g/L. In a specific embodiment, Taub's
media is supplemented with a wheat hydrolysate. In another specific
embodiment, Taub's media is supplemented with a wheat hydrolysate
at a final concentration of 2.5 g/L. The present invention provides
a serum-free media referred to herein as MediV SFM 101 comprising
Taub's media supplemented with a wheat hydrolysate at a final
concentration of 2.5 g/L.
In another embodiment, Taub's media is supplemented with a lipid
mixture at a final concentration of at least 50%, or at least 60%,
or at least 70%, or at least 80%, or at least 90%, or at least
100%, or at least 125%, or at least 150%, or at least 200%, or at
least 300% of the manufacturers recommended final concentration. In
a specific embodiment, Taub's media is supplemented with a
chemically defined lipid mixture. In another specific embodiment,
Taub's media is supplemented with a chemically defined lipid
mixture at a final concentration of 100% of the manufacturers
recommended final concentration (e.g., a 100.times. stock obtained
from a manufacture would be add to the media to a final
concentration of 1.times.). The present invention provides a
serum-free media referred to herein as MediV SFM 102 comprising
Taub's media supplemented with a chemically defined lipid mixture
at a final concentration of 100% of the manufacturers recommended
final concentration.
In still another embodiment, Taub's media is supplemented with a
plant hydrolysate at a final concentration of at least 0.5 g/L, or
at least 1.0 g/L, or at least 1.5 g/L, or at least 2.0 g/L, or at
least 2.5 g/L, or at least 3.0 g/L, or at least 5.0 g/L, or at
least 10 g/L, or at least 20 g/L and with a lipid mixture at a
final concentration of at least 50%, or at least 60%, or at least
70%, or at least 80%, or at least 90%, or at least 100%, or at
least 125%, or at least 150%, or at least 175%, or at least 200% of
the manufacturers recommended concentration. In a specific
embodiment, Taub's media is supplemented with wheat hydrolysate and
a chemically defined lipid mixture. In another specific embodiment,
Taub's media is supplemented with a wheat hydrolysate at a final
concentration of 2.5 g/L and a chemically defined lipid mixture at
a final concentration of 100% of the manufacturers recommended
final concentration. The present invention provides a serum-free
media referred to herein as MediV SFM 103 comprising Taub's media
supplemented with a wheat hydrolysate at a final concentration of
2.5 g/L and a chemically defined lipid mixture at a final
concentration of 100% of the manufacturers recommended final
concentration.
In yet another embodiment, Taub's media is supplemented with a
growth hormone. Growth hormones which may be used include but are
not limited to, Epidermal Growth Factor (EGF), Insulin Growth
Factor (IGF), Transforming Growth Factor (TGF) and Fibroblast
Growth Factor (FGF). In a particular embodiment, the growth hormone
is Epidermal Growth Factor (EGF). In one embodiment, Taub's media
is supplemented with a growth factor at a final concentration of
between about 0.1 to about 50.0 ng/ml, or between about 0.5 to
about 25.0 ng/ml, or between about 1.0 to about 20 ng/ml, or
between about 5.0 to about 15.0 ng/ml, or between about 8 ng/ml to
about 12 ng/ml. In a specific embodiment, Taub's media is
supplemented with a EGF at a final concentration of about 10 ng/ml.
In still other embodiments, Taub's media is supplemented with a
growth factor at a final concentration of between about 0.1 to
about 50.0 ng/ml, or between about 0.5 to about 25.0 ng/ml, or
between about 1.0 to about 20 ng/ml, or between about 5.0 to about
15.0 ng/ml, or between about 8 ng/ml to about 12 ng/ml and with a
plant hydrolysate at a final concentration of at least 0.5 g/L, or
at least 1.0 g/L, or at least 1.5 g/L, or at least 2.0 g/L, or at
least 2.5 g/L, or at least 3.0 g/L, or at least 5.0 g/L, or at
least 10 g/L, or at least 20 g/L and with a lipid mixture at a
final concentration of at least 50%, or at least 60%, or at least
70%, or at least 80%, or at least 90%, or at least 100%, or at
least 125%, or at least 150%, or at least 175%, or at least 200% of
the manufacturers recommended concentration. In another specific
embodiment, Taub's media is supplemented with a wheat hydrolysate
at a final concentration of 2.5 g/L and a chemically defined lipid
mixture at a final concentration of 100% of the manufacturers
recommended final concentration and EGF at a final concentration of
about 10 ng/ml. The present invention provides a serum-free media
referred to herein as MediV SFM 104 comprising Taub's media
supplemented with a wheat hydrolysate at a final concentration of
2.5 g/L and a chemically defined lipid mixture at a final
concentration of 100% of the manufacturers recommended final
concentration and EGF at a final concentration of about 10
ng/ml.
It will also be appreciated by one skilled in the art that animal
protein-free media formulations may be desirable for the production
of virus used in the manufacture of vaccines. Accordingly, in
certain embodiments one or more or all of the animal derived
components of the serum-free media disclosed herein (e.g., MediV
SF101, MediV SF102, MediV SF103, MediV SF104 and Medi SF105) is
replaced by an animal-free derivative. For example, commercially
available recombinant insulin derived from non-animal sources
(e.g., Biological Industries Cat. No. 01-818-1) may utilized
instead of insulin derived from an animal source. Likewise, iron
binding agents (see, e.g., U.S. Pat. Nos. 5,045,454; 5,118,513;
6,593,140; and PCT publication number WO 01/16294) may be utilized
instead of transferrin derived from an animal source. In one
embodiment, serum-free media formulations of the invention comprise
tropolone (2-hydroxy-2,4,6-cyclohepatrien-1) and a source of iron
(e.g., ferric ammonium citrate, ferric ammonium sulphate) instead
of transferrin. For example, tropolone or a tropolone derivative
will be present in an excess molar concentration to the iron
present in the medium for at a molar ratio of about 5 to 1 to about
70 to 1, or of about 10 to 1 to about 70 to 1. Accordingly, where
the iron concentration in the medium is around 0.3 .mu.M, the
tropolone or derivative thereof may be employed at a concentration
of about 1.5 .mu.M to about 20 .mu.M, e.g. about 3 .mu.M to about
20 .mu.M. The iron may be present as ferrous or ferric ions, for
example resulting from the use of simple or complex iron salts in
the medium such as ferrous sulphate, ferric chloride, ferric
nitrate or in particular ferric ammonium citrate. The present
invention provides a serum-free media referred to herein as MediV
SFM 105 comprising Taub's media without transferrin supplemented
with a wheat hydrolysate at a final concentration of 2.5 g/L and a
chemically defined lipid mixture at a final concentration of 100%
of the manufacturers recommended final concentration and EGF at a
final concentration of about 10 ng/ml and Ferric ammonium
citrate:Tropolone or Ferric ammonium sulfate:Tropolone at a ratio
of between 10 to 1 and 70 to 1.
In one embodiment, MDCK-SF101, MDCK-SF102, MDCK-SF103, MDCK-SF104
and MDCK-SF105 serum-free adapted non-tumorigenic cells
(collectively referred to herein as MDCK-SF) are derived from Madin
Darby Canine Kidney Cells (MDCK) cells obtained from the American
type Culture Collection (ATCC CCL34) by culturing in a chemically
defined media supplemented with serum for at least one passage and
then passaging them in a serum-free media such as, for example, the
serum-free medias described supra. In a specific embodiment, MDCK
cells (ATCC CCL34) are adapted to serum-free media to generate a
MDCK-SF cell line as follows: The MDCK (ATCC CCL34) cells are
passaged in Dulbecco's Modified Eagle Medium (DMEM) supplemented
with fetal bovine serum (10% v/v), 4 mM glutamine and 4.5 g/L
glucose at least once and then passaged in serum-free media. The
MDCK-SF cells are then passaged as needed in serum-free media to
obtain enough cell to prepare a frozen pre Master Cell Bank
(PreMCB). In certain embodiments, the cells are passaged in a serum
containing media (e.g., Dulbecco's Modified Eagle Medium (DMEM)
supplemented with fetal bovine serum (10% v/v), 4 mM glutamine and
4.5 g/L glucose) between 1 and 5 times, or between 4 and 10 time,
or between 9 and 20 times, or more than 20 times, and then passaged
in serum-free media (e.g., MediV SF101, MediV SF102, MediV SF103,
MediV SF104 and Medi SF105).
It is specifically contemplated that the MDCK-SF serum-free adapted
cells are passaged for another 20 passages or more, from a vial of
PreMCB and tested for tumorigenicity in an vivo adult nude mice
model and karyology in a karyotype assay. In certain embodiments,
the expanded MDCK-SF cells will not produce nodules when injected
subcutaneously into adult nude mice and/or will have a modal
chromosome number of 78. In another embodiment, the expanded
MDCK-SF cells will have a modal chromosome number of 78 with a
range of chromosome numbers of no more then about 60 to about 88,
or of no more then about 65 to about 85, or of no more then about
65-80, or of no more then about 70 to about 85. In one embodiment,
the MDCK-SF cells are non-tumorigenic after at least 20 passages,
or after at least 30 passages, or after at least 40 passages, or
after at least 50 passages, or after at least 60 passages, or after
at least 70 passages, or after at least 80 passages, or after at
least 90 passages, or after at least 100 passages in a medium
(e.g., a media described herein).
In one embodiment, the serum-free media used for the derivation of
MDCK-SF cells is MediV SF101. In another embodiment, the serum-free
media used for the derivation of MDCK-SF cells is MediV SF102. In
yet another embodiment, the serum-free media used for the
derivation of MDCK-SF cells is MediV SF103. In still another
embodiment, the serum-free media used for the derivation of MDCK-SF
cells is MediV-SF104. In another embodiment, the serum-free media
used for the derivation of MDCK-SF cells is MediV SF105. In yet
another embodiment, the serum-free media used for the derivation of
MDCK-SF cells is an APF media. It is contemplated that the media
described herein may be formulated to eliminate animal proteins.
For example bovine transferrin may be replaced with a recombinant
transferrin derived from a non animal source.
Culture Conditions
The present invention provides methods for the cultivation of MDCK
cells (preferably non-tumorigenic) and other animal cells
(tumorigenic or not) in serum containing and serum-free media
formulations (supra). It is specifically contemplated that
additional culture conditions may play a role in the maintenance of
the MDCK-S and MDCK-SF cells in a non-tumorigenic state. These
culture conditions include but are not limited to the choice of
adherent surface, cell density, temperature, CO.sub.2
concentration, method of cultivation, dissolved oxygen content and
pH.
It is specifically contemplated that one skilled in the art may
adapt the culture conditions in a number of ways to optimize the
growth of the MDCK cells of the invention. Such adaptations may
also result in a increase in the production of viral material
(e.g., virus), alternatively, one skilled in the art may adapt the
culture conditions to optimize the production of vaccine material
from the MDCK cells of the invention without regard for the growth
of the cells. These culture conditions include but are not limited
to adherent surface, cell density, temperature, CO.sub.2
concentration, method of cultivation, dissolved oxygen content and
pH.
In one embodiment, the MDCK cells of the invention are cultivated
as adherent cells on a surface to which they attach. Adherent
surfaces on which tissue culture cells can be grown on are well
known in the art. Adherent surfaces include but are not limited to,
surface modified polystyrene plastics, protein coated surfaces
(e.g., fibronectin and/or collagen coated glass/plastic) as well as
a large variety of commercially available microcarriers (e.g.,
DEAE-Dextran microcarrier beads, such as Dormacell, Pfeifer &
Langen; Superbead, Flow Laboratories; styrene
copolymer-tri-methylamine beads, such as Hillex, SoloHill, Ann
Arbor). Microcarrier beads are small spheres (in the range of
100-200 microns in diameter) that provide a large surface area for
adherent cell growth per volume of cell culture. For example a
single liter of medium can include more than 20 million
microcarrier beads providing greater than 8000 square centimeters
of growth surface. The choice of adherent surface is determined by
the methods utilized for the cultivation of the MDCK cells of the
invention and can be determined by one skilled in the art. Suitable
culture vessels which can be employed in the course of the process
according to the invention are all vessels known to the person
skilled in the art, such as, for example, spinner bottles, roller
bottles, fermenters or bioreactors. For commercial production of
viruses, e.g., for vaccine production, it is often desirable to
culture the cells in a bioreactor or fermenter. Bioreactors are
available in volumes from under 1 liter to in excess of 100 liters,
e.g., Cyto3 Bioreactor (Osmonics, Minnetonka, Minn.); NBS
bioreactors (New Brunswick Scientific, Edison, N.J.); laboratory
and commercial scale bioreactors from B. Braun Biotech
International (B. Braun Biotech, Melsungen, Germany).
In one embodiment, the MDCK cells of the invention are cultivated
as adherent cells in a batch culture system. In still another
embodiment, the MDCK cells of the invention are cultivated as
adherent cells in a perfusion culture system. It is specifically
contemplated that the MDCK cells of the invention will be cultured
in a perfusion system, (e.g., in a stirred vessel fermenter, using
cell retention systems known to the person skilled in the art, such
as, for example, centrifugation, filtration, spin filters and the
like) for the production of vaccine material (e.g., virus).
In one embodiment, the MDCK cells of the invention are cultivated
at a CO.sub.2 concentration of at least 1%, or of at least 2%, or
of at least 3%, or of at least 4%, or of at least 5%, or of at
least 6%, or of at least 7%, or of at least 8%, or of at least 9%,
or of at least 10%, or of at least 20%.
In one embodiment the dissolved oxygen (DO) concentration (pO.sub.2
value) is advantageously regulated during the cultivation of the
MDCK cells of the invention and is in the range from 5% and 95%
(based on the air saturation), or between 10% and 60%. In a
specific embodiment the dissolved oxygen (DO) concentration
(pO.sub.2 value) is at least 10%, or at least 20%, or at least 30%,
or at least 50%, or at least 60%.
In another embodiment, the pH of the culture medium used for the
cultivation of the MDCK cells of the invention is regulated during
culturing and is in the range from pH 6.4 to pH 8.0, or in the
range from pH 6.8 to pH 7.4. In a specific embodiment, the pH of
the culture medium is at least 6.4, or at least 6.6, or at least
6.8, or at least 7.0, or at least 7.2, or at least 7.4, or at least
7.6, or at least 7.8, or at least 8.0.
In a further embodiment, the MDCK cells of the invention are
cultured at a temperature of 25.degree. C. to 39.degree. C. It is
specifically contemplated that the culture temperature may be
varied depending on the process desired. For example, the MDCK
cells of the invention may be grown at 37.degree. C. for
proliferation of the cells and at a lower temperature (e.g.,
25.degree. C. to 35.degree. C.) of for the production of vaccine
material (e.g., virus). In another embodiment, the cells are
cultured at a temperature of less than 30.degree. C., or of less
than 31.degree. C., or of less than 32.degree. C., or of less than
33.degree. C., or of less than 34.degree. C. for the production of
vaccine material. In another embodiment, the cells are cultured at
a temperature of 30.degree. C., or 31.degree. C., or 32.degree. C.,
or 33.degree. C., or 34.degree. C. for the production of vaccine
material.
In order to generate vaccine material (e.g., virus) it is
specifically contemplated that the MDCK cells of the invention are
cultured such that the medium can be readily exchanged (e.g., a
perfusion system). The cells may be cultured to a very high cell
density, for example to between 1.times.10.sup.6 and
25.times.10.sup.6 cells/mL. The content of glucose, glutamine,
lactate, as well as the pH and pO.sub.2 value in the medium and
other parameters, such as agitation, known to the person skilled in
the art can be readily manipulated during culture of the MDCK cells
of the invention such that the cell density and/or virus production
can be optimized.
Production of Vaccine Material (e.g., Virus)
The present invention provides a process for the production of
viruses in cell culture (referred to hereinafter as "the process of
the invention"), in which the MDCK cells of the invention are used.
In one embodiment the process comprises the following steps: i)
proliferation of the MDCK cells of the present invention in culture
media; ii) infection of the cells with virus; and iii) after a
further culturing phase, isolating the viruses replicated in the
non-tumorigenic cells.
In one embodiment the MDCK cells of the invention are proliferated
in step (i) as adherent cells. The MDCK cells of the invention can
be cultured in the course of the process in any media including,
but not limited to, those described supra. In certain embodiments,
the MDCK cells of the invention are cultured in the course of the
process in a serum-free medium such as, for example, MediV-SF101,
MediV-SF102, MediV-SF103, MediV-SF104, MediV-SF105 and APF
formulations thereof. Optionally, the MDCK cells of the invention
can be cultured in the course of the process in a serum containing
media (e.g., DMEM+10% FBS+4 mM glutamine+4.5 g/L glucose).
Additional culture conditions such as, for example, temperature,
pH, pO.sub.2, CO.sub.2 concentration, and cell density are
described in detail supra. One skilled in the art can establish a
combination of culture conditions for the proliferation of the MDCK
cells of the invention for the production of virus.
The temperature for the proliferation of the cells before infection
with viruses is in one embodiment between 22.degree. C. and
40.degree. C. In certain embodiments, the temperature for the
proliferation of the cells before infection with viruses is less
then 39.degree. C., or less than 38.degree. C., or less than
37.degree. C., or less than 36.degree. C., or less than 35.degree.
C., or less than 34.degree. C., or less than 33.degree. C., or less
than 32.degree. C., or less than 30.degree. C., or less than
28.degree. C., or less than 26.degree. C., or less than 24.degree.
C. Culturing for proliferation of the cells (step (i)) is carried
out in one embodiment of the process in a perfusion system, e.g. in
a stirred vessel fermenter, using cell retention systems known to
the person skilled in the art, such as, for example,
centrifugation, filtration, spin filters, microcarriers, and the
like.
The cells are in this case proliferated for 1 to 20 days, or for 3
to 11 days. Exchange of the medium is carried out in the course of
this, increasing from 0 to approximately 1 to 5 fermenter volumes
per day. The cells are proliferated up to high cell densities in
this manner, for example up to at least
1.times.10.sup.6-25.times.10.sup.6 cells/mL. The perfusion rates
during culture in the perfusion system can be regulated via the
cell count, the content of glucose, glutamine or lactate in the
medium and via other parameters known to the person skilled in the
art. Alternatively, the cells in step (i) of the process according
to the invention be cultured in a batch process.
In one embodiment of the process according to the invention, the
pH, pO.sub.2 value, glucose concentration and other parameters of
the culture medium used in step (i) is regulated during culturing
as described above using methods known to the person skilled in the
art.
In another embodiment, the infection of the cells with virus is
carried out at an m.o.i. (multiplicity of infection) of about
0.0001 to about 10, or about 0.0005 to about 5, or about 0.002 to
about 0.5. In still another embodiment, the infection of the cells
with virus is carried out at an m.o.i. (multiplicity of infection)
of 0.0001 to 10, or 0.0005 to 5, or 0.002 to 0.5. After infection,
the infected cell culture is cultured further to replicate the
viruses, in particular until a maximum cytopathic effect or a
maximum amount of virus antigen can be detected. In one embodiment,
after infection the cells are cultured at a temperature of between
22.degree. C. and 40.degree. C. In certain embodiments, after
infection with viruses the cells are cultured at a temperature of
less then 39.degree. C., or less than 38.degree. C., or less than
37.degree. C., or less than 36.degree. C., or less than 35.degree.
C., or less than 34.degree. C., or less than 33.degree. C., or less
than 32.degree. C., or less than 30.degree. C., or less than
28.degree. C., or less than 26.degree. C., or less than 24.degree.
C. In another embodiment, after infection the cells are cultured at
a temperature of less than 33.degree. C. In still another
embodiment, after infection the cells are cultured at a temperature
of 31.degree. C. In certain embodiments, the culturing of the cells
is carried out for 2 to 10 days. The culturing can be carried out
in the perfusion system or optionally in the batch process.
The culturing of the cells after infection with viruses (step
(iii)) is in turn carried out such that the pH and pO.sub.2 value
are maintained as described above. During the culturing of the
cells or virus replication according to step (iii) of the process,
a substitution of the cell culture medium with freshly prepared
medium, medium concentrate or with defined constituents such as
amino acids, vitamins, lipid fractions, phosphates etc. for
optimizing the antigen yield is also possible. The cells can either
be slowly diluted by further addition of medium or medium
concentrate over several days or can be incubated during further
perfusion with medium or medium concentrate. The perfusion rates
can in this case in turn be regulated by means of the cell count,
the content of glucose, glutamine, lactate or lactate dehydrogenase
in the medium or other parameters known to the person skilled in
the art. A combination of the perfusion system with a fed-batch
process is further possible.
In one embodiment of the process, the harvesting and isolation of
the produced viruses (step (iii)) is carried out after a sufficient
period to produce suitable yields of virus, such as 2 to 10 days,
or optionally 3 to 7 days, after infection. In one embodiment of
the process, the harvesting and isolation of the produced viruses
(step (iii)) is carried out 2 days, or 3 days, or 4 days, or 5
days, or after 6 days, or 7 days, or 8 days, or 9 days, or 10 days,
after infection.
Viruses which may be produced in the MDCK cells of the present
invention include but are not limited to, animal viruses, including
families of Orthomyxoviridae, Paramyxoviridae, Togaviridae,
Herpesviridae, Rhabdoviridae, Retroviridae, Reoviridae,
Flaviviridae, Adenoviridae, Picornaviridae, Arenaviridae and
Poxyiridae.
Systems for producing influenza viruses in cell culture have also
been developed in recent years (See, e.g., Furminger. in Textbook
of Influenza, ed Nicholson, Webster and Hay, pp. 324-332, Blackwell
Science (1998); Merten et al. in Novel Strategies in The Design and
Production of Vaccines, ed Cohen & Shafferman, pp. 141-151,
Kluwer Academic (1996)). Typically, these methods involve the
infection of suitable immortalized host cells with a selected
strain of virus. While eliminating many of the difficulties related
to vaccine production in hen's eggs, not all pathogenic strains of
influenza grow well and can be produced according to established
tissue culture methods. In addition, many strains with desirable
characteristics, e.g., attenuation, temperature sensitivity and
cold adaptation, suitable for production of live attenuated
vaccines, have not been successfully grown, especially at
commercial scale, in tissue culture using established methods.
The present invention provides several non-tumorigenic MDCK cell
lines, which have been adapted to grow in either serum containing
or serum-free medias and which are capable of supporting the
replication of viruses including but not limited to influenza when
cultured. These cells lines are suitable for the economical
replication of viruses in cell culture for use as vaccine material.
The MDCK cells of the present invention are particularly useful for
the production of cold adapted, temperature sensitive (ca/ts)
strains of influenza (e.g., the influenza strains found in
FluMist.RTM.) which do not grow well using other established cell
lines (see, Example 1, infra). Further, the MDCK cells of the
present invention are useful for the production of strains of
influenza which may not grow in embryonated eggs such as avian
influenza viruses which can also cause disease in humans (e.g., a
"pandemic" strains)
Influenza viruses which may be produced by the process of the
invention in the MDCK cells of the invention include but are not
limited to, reassortant viruses that incorporate selected
hemagglutinin and/or neuramimidase antigens in the context of an
attenuated, temperature sensitive, cold adapted (ca/ts/at) master
strain. For example, viruses can comprise the backbones (or one or
more vRNA segment) of master strains that are one or more of, e.g.,
temperature-sensitive (ts), cold-adapted (ca), or an attenuated
(att) (e.g., A/Ann Arbor/6/60, B/Ann Arbor/1/66, PR8,
B/Leningrad/14/17/55, B/14/5/1, B/USSR/60/69, B/Leningrad/179/86,
B/Leningrad/14/55, B/England/2608/76 etc.). Methods for the
production of reassortant influenza vaccine strains in either eggs
or cell lines are known in the art and include, for example,
Kilbourne, E. D. in Vaccines (2.sup.nd Edition), ed. Plotkin and
Mortimer, WB Saunders Co. (1988) and those disclosed in PCT
Application PCT Patent Publication Nos. WO 05/062820 and WO
03/091401. Other influenza viruses which may be produced by the
process of the invention in the MDCK cells of the invention include
recombinant influenza viruses which may express a heterologous gene
product, see for example, U.S. Patent Publication Nos. 2004/0241139
and 2004/0253273.
In one embodiment, the cells are proliferated (step (i)) as
described supra, the cells are then infected with influenza viruses
(step (ii)). In certain embodiments, the infection is carried out
at an m.o.i. (multiplicity of infection) of 0.0001 to 10, or of
0.0005 to 5, or of 0.002 to 0.5. In other embodiments, the
infection is carried out at an m.o.i. (multiplicity of infection)
of about 0.0001 to about 10, or of about 0.0005 to about 5, or of
about 0.002 to about 0.5. Optionally a protease is added which
brings about the cleavage of the precursor protein of hemagglutinin
[HA.sub.0] and thus the adsorption of the viruses on the cells. The
addition of a protease can be carried out according to the
invention shortly before, simultaneously to or shortly after the
infection of the cells with influenza viruses (step (ii)). If the
addition is carried out simultaneously to the infection, the
protease can either be added directly to the cell culture to be
infected or, for example, as a concentrate together with the virus
inoculate. The protease is, in certain aspects of the invention, a
serine protease, or a cysteine protease, or an asparagine protease.
In one embodiment, trypsin is used. In a specific embodiment,
TPCK-treated trypsin is used.
In one embodiment, trypsin is added to the cell culture up to a
final concentration of 1 to 5000 mU/ml, or 5 to 1000 mU/ml, or 100
to 500 mU/ml. In an alternative embodiment, trysin is added to the
cell culture up to a final concentration of 1 to 200 .mu.g/ml, or 5
to 50 .mu.g/ml, or 5 to 30 .mu.g/ml in the culture medium. During
the further culturing of the infected cells according to step (iii)
of the process according to the invention, trypsin reactivation can
be carried out by fresh addition of trypsin in the case of the
batch process or in the case of the perfusion system by continuous
addition of a trypsin solution or by intermittent addition.
After infection, the infected cell culture is cultured further to
replicate the viruses, in particular until a maximum cytopathic
effect or a maximum amount of virus and/or virus antigen can be
detected. In certain embodiments, the culturing of the cells is
carried out for 2 to 10 days. The culturing can in turn be carried
out in the perfusion system or optionally in the batch process. In
a further embodiment, the cells are cultured at a temperature of
25.degree. C. to 36.degree. C., or of 29.degree. C. to 34.degree.
C., after infection with influenza viruses. The culturing of the
infected cells at temperatures below 33.degree. C., in particular
in the temperature ranges indicated above, leads to the production
of higher yields of certain influenza viruses, such as, for example
B strains. Furthermore, the culturing of the infected cells at
temperatures below 35.degree. C. is contemplated for the production
of temperature sensitive, cold adapted (ts/ca) influenza virus. It
is contemplated that ts/ca viruses may also be attenuated (att). In
another embodiment, the cells are cultured at a temperature of less
than 30.degree. C., or of less than 31.degree. C., or of less than
32.degree. C., or of less than 33.degree. C., or of less than
34.degree. C. for the production of ts/ca influenza strains. In a
specific embodiment, the cells are cultured at a temperature of
31.degree. C., for the production of influenza virus B strains.
The culturing of the cells after infection with influenza viruses
(step (iii)) is in turn carried out, for example, as described
supra
In one embodiment of the process, the harvesting and isolation of
the produced influenza viruses (step (iii)) is carried out after a
sufficient period to produce suitable yields of virus, such as 2 to
10 days, or 3 to 7 days, after infection. Viruses are typically
recovered from the culture medium, in which infected cells have
been grown. Typically crude medium is clarified prior to
concentration of influenza viruses. Common methods include
filtration, ultrafiltration, adsorption on barium sulfate and
elution, and centrifugation. For example, crude medium from
infected cultures can first be clarified by centrifugation at,
e.g., 1000-2000.times.g for a time sufficient to remove cell debris
and other large particulate matter, e.g., between 10 and 30
minutes. Alternatively, the medium is filtered through a 0.8 .mu.m
cellulose acetate filter to remove intact cells and other large
particulate matter. Optionally, the clarified medium supernatant is
then centrifuged to pellet the influenza viruses, e.g., at
15,000.times.g, for approximately 3-5 hours. Following resuspension
of the virus pellet in an appropriate buffer, such as STE (0.01 M
Tris-HCl; 0.15 M NaCl; 0.0001 M EDTA) or phosphate buffered saline
(PBS) at pH 7.4, the virus may be concentrated by density gradient
centrifugation on sucrose (60%-12%) or potassium tartrate
(50%-10%). Either continuous or step gradients, e.g., a sucrose
gradient between 12% and 60% in four 12% steps, are suitable. The
gradients are centrifuged at a speed, and for a time, sufficient
for the viruses to concentrate into a visible band for recovery.
Alternatively, and for most large scale commercial applications,
virus is elutriated from density gradients using a zonal-centrifuge
rotor operating in continuous mode. Additional details sufficient
to guide one of skill through the preparation of influenza viruses
from tissue culture are provided, e.g., in Furminger, in Textbook
of Influenza pp. 324-332 Nicholson et al. (ed); Merten et al., in
Novel Strategies in Design and Production of Vaccines pp. 141-151
Cohen & Shafferman (ed), and U.S. Pat. No. 5,690,937. If
desired, the recovered viruses can be stored at -80.degree. C. in
the presence of a stabilizer, such as sucrose-phosphate-glutamate
(SPG).
In certain embodiments of the process, the virus is treated with
Benzonase.RTM. or other a non-specific endonuclease. Optionally,
the Benzonase.RTM. treatment occurs early in the harvesting and
isolation of the produced influenza viruses (step (iii)). In other
embodiments of the process, following Benzonase.RTM. treatment, the
material is clarified. Methods useful for clarification include but
are not limited to, direct flow filtration (DFF). Additional steps
which may be utilized for the harvesting and isolation of the
produced influenza virus (step(iii)) include but are not limited
to, tangential flow filtration (TFF), affinity chromatography as
well as ion-exchange chromatography and/or hydroxyapatite
chromatography. Other steps are exemplified in the Examples section
infra.
Vaccine Compositions and Methods of Use
The invention further relates to viruses (e.g., influenza) which
are obtainable by a process of the invention. These viruses can be
formulated by known methods to provide a vaccine for administration
to humans or animals. The viruses can be present as intact virus
particles (e.g., live attenuated viruses) or as
inactive/disintegrated virus (e.g., treated with detergents of
formaldehyde). Optionally, a defined viral component (e.g.,
protein) may be isolated from the viruses by methods know to the
person skilled in the art, and used in the preparation of a
vaccine.
The formulation of intact virus particles (e.g., live attenuated
viruses) may include additional steps including, but not limited
to, a buffer exchange by filtration into a final formulation
followed by a sterilization step. Buffers useful for such a
formulation may contain 200 mM sucrose and a phosphate or histidine
buffer of pH 7.0-7.2 with the addition of other amino acid
excipients such as arginine. In certain embodiments, stabilization
protein hydrolysates such as porcine gelatin are added. In some
embodiments, the final viral solutions/vaccines of the invention
can comprise live viruses that are stable in liquid form for a
period of time sufficient to allow storage "in the field" (e.g., on
sale and commercialization when refrigerated at 2-8.degree. C.,
4.degree. C., 5.degree. C., etc.) throughout an influenza
vaccination season (e.g., typically from about September through
March in the northern hemisphere). Thus, the virus/vaccine
compositions are desired to retain their potency or to lose their
potency at an acceptable rate over the storage period. In other
embodiments, such solutions/vaccines are stable in liquid form at
from about 2.degree. C. to about 8.degree. C., e.g., refrigerator
temperature. For example, methods and compositions for formulating
a refrigerator stable attenuated influenza vaccine are described in
PCT Patent Application PCT/US2005/035614 filed Oct. 4, 2005, also
see PCT Publication WO 05/014862. Optionally, spray drying, a rapid
drying process whereby the formulation liquid feed is spray
atomized into fine droplets under a stream of dry heated gas, may
be utilized to extend storage time of a vaccine formulation. The
evaporation of the fine droplets results in dry powders composed of
the dissolved solutes (see, e.g., US Patent Publication
2004/0042972). Methods for the generation and formulation of
inactive/disintegrated virus particles for vaccine compositions are
well known in the art and have been utilized for over 40 years.
Generally, virus or viral components can be administered
prophylactically in an appropriate carrier or excipient to
stimulate an immune response specific for one or more strains of
virus. Typically, the carrier or excipient is a pharmaceutically
acceptable carrier or excipient, such as sterile water, aqueous
saline solution, aqueous buffered saline solutions, aqueous
dextrose solutions, aqueous glycerol solutions, ethanol or
combinations thereof. The preparation of such solutions insuring
sterility, pH, isotonicity, and stability is effected according to
protocols established in the art. Generally, a carrier or excipient
is selected to minimize allergic and other undesirable effects, and
to suit the particular route of administration, e.g., subcutaneous,
intramuscular, intranasal, etc.
Optionally, the formulation for prophylactic administration of the
viruses, or components thereof, also contains one or more adjuvants
for enhancing the immune response to the influenza antigens.
Suitable adjuvants include: saponin, mineral gels such as aluminum
hydroxide, surface active substances such as lysolecithin, pluronic
polyols, polyanions, peptides, oil or hydrocarbon emulsions,
bacille Calmette-Guerin (BCG), Corynebacterium parvum, and the
synthetic adjuvants QS-21 and MF59.
Generally, vaccine formulations are administered in a quantity
sufficient to stimulate an immune response specific for one or more
strains of influenza virus. Preferably, administration of the
viruses elicits a protective immune response. Dosages and methods
for eliciting a protective immune response against one or more
viral strain are known to those of skill in the art. For example,
inactivated influenza viruses are provided in the range of about
1-1000 HID.sub.50 (human infectious dose), i.e., about
10.sup.5-10.sup.8 pfu (plaque forming units) per dose administered.
Alternatively, about 10-50 .mu.g, e.g., about 15 .mu.g HA is
administered without an adjuvant, with smaller doses being
administered with an adjuvant. Typically, the dose will be adjusted
within this range based on, e.g., age, physical condition, body
weight, sex, diet, time of administration, and other clinical
factors. The prophylactic vaccine formulation is systemically
administered, e.g., by subcutaneous or intramuscular injection
using a needle and syringe, or a needleless injection device.
Alternatively, the vaccine formulation is administered
intranasally, either by drops, large particle aerosol (greater than
about 10 microns), or spray into the upper respiratory tract. While
any of the above routes of delivery results in a protective
systemic immune response, intranasal administration confers the
added benefit of eliciting mucosal immunity at the site of entry of
the influenza virus. For intranasal administration, attenuated live
virus vaccines are often preferred, e.g., an attenuated, cold
adapted and/or temperature sensitive recombinant or reassortant
influenza virus. While stimulation of a protective immune response
with a single dose is preferred, additional dosages can be
administered, by the same or different route, to achieve the
desired prophylactic effect. These methods can be adapted for any
virus including but not limited to, orthomyxoviruses (including
influenza A and B strains), paramyxoviruses (including RSV, human
metapneumovirus and parainfluenza), rhabdoviruses and
flavoviruses.
Influenza Virus
The methods, processes and compositions herein primarily concerned
with production of influenza viruses for vaccines. Influenza
viruses are made up of an internal ribonucleoprotein core
containing a segmented single-stranded RNA genome and an outer
lipoprotein envelope lined by a matrix protein. Influenza A and
influenza B viruses each contain eight segments of single stranded
negative sense RNA. The influenza A genome encodes eleven
polypeptides. Segments 1-3 encode three polypeptides, making up a
RNA-dependent RNA polymerase. Segment 1 encodes the polymerase
complex protein PB2. The remaining polymerase proteins PB1 and PA
are encoded by segment 2 and segment 3, respectively. In addition,
segment 1 of some influenza strains encodes a small protein,
PB1-F2, produced from an alternative reading frame within the PB1
coding region. Segment 4 encodes the hemagglutinin (HA) surface
glycoprotein involved in cell attachment and entry during
infection. Segment 5 encodes the nucleocapsid nucleoprotein (NP)
polypeptide, the major structural component associated with viral
RNA. Segment 6 encodes a neuramimidase (NA) envelope glycoprotein.
Segment 7 encodes two matrix proteins, designated M1 and M2, which
are translated from differentially spliced mRNAs. Segment 8 encodes
NS1 and NS2, two nonstructural proteins, which are translated from
alternatively spliced mRNA variants.
The eight genome segments of influenza B encode 11 proteins. The
three largest genes code for components of the RNA polymerase, PB1,
PB2 and PA. Segment 4 encodes the HA protein. Segment 5 encodes NP.
Segment 6 encodes the NA protein and the NB protein. Both proteins,
NB and NA, are translated from overlapping reading frames of a
biscistronic mRNA. Segment 7 of influenza B also encodes two
proteins: M1 and M2. The smallest segment encodes two products, NS1
which is translated from the full length RNA, and NS2 which is
translated from a spliced mRNA variant.
Reassortant viruses are produced to incorporate selected
hemagglutinin and neuraminidase antigens in the context of an
approved master strain also called a master donor virus (MDV).
FluMist.RTM. makes use of approved cold adapted, attenuated,
temperature sensitive MDV strains (e.g., A/AnnArbor/6/60 and B/Ann
Arbor/1/66). A number of methods are useful for the generation of
reassortant viruses including egg-based methods and more recently
cell culture methods See, e.g., PCT Publications WO 03/091401; WO
05/062820 and U.S. Pat. Nos. 6,544,785; 6,649,372; 6,951,754). It
is contemplated that the MDCK cells, media and processes of the
invention are useful for the production of influenza viruses
including, but not limited to, the influenza strains disclosed
herein (e.g., A/AnnArbor/6/60 and B/AnnArbor/1/66) and reassortant
viruses comprising genes of the A/AnnArbor/6/60, B/AnnArbor/1/66,
PR8. It is further contemplated that that the MDCK cells, media and
processes of the invention are useful for the production of
influenza viruses, including reassortant viruses, having one or
more of the following phenotypes, temperature sensitive, cold
adapted, attenuated. Reassortants may be generated by classical
reassortant techniques, for example by co-infection methods or
optionally by plasmid rescue techniques (see, e.g., PCT
Publications WO 03/091401; WO 05/062820 and U.S. Pat. Nos.
6,544,785; 6,649,372, 6,951,754).
EXAMPLES
The invention is now described with reference to the following
examples. These examples are provided for the purpose of
illustration only and the invention should in no way be construed
as being limited to these examples but rather should be construed
to encompass any and all variations which become evident as a
result of the teachings provided herein.
Example 1
Determination of Spread of Infection of ca/ts Influenza Strains in
Cell Lines and Characterization of Influenza Produced in MDCK
Cells
There has been an effort by the vaccine industry to develop
alternative production platforms that do not utilize eggs and to
produce influenza vaccines in a mammalian or insect cell culture
system. The obvious advantages are easy scalability, increased
process control and removal of egg proteins that could cause
allergic reaction in some vaccines. Since cell culture based
systems can be rapidly scaled up, it offers an additional advantage
at the time of a influenza pandemic, when there is a potential for
shortage of supply of eggs and rapid production of vaccine is
required. Initial studies have been performed with a total of 7
different cell lines: 2 human diploid lung fibroblast lines (MRC-5
and WI-38) (data not shown), a human retinoblastoma and a human
kidney cell line both of which were genetically constructed for
production of adenoviral products (PER.C6 and 293, respectively)
(data not shown), a fetal rhesus lung cell line (FRhL2) (data not
shown), an African green monkey kidney cell line (Vero), and a
Marin-Darby canine kidney cell line (MDCK). MDCK cells were the
only cell line of those tested to be capable of propagating all
four types of cold adapted, temperature sensitive attenulated
(ca/ts/att) reassortant influenza virus strains, H1N1, H3N2, the
potential pandemic vaccine strain H5N1, as well as B strains, to
commercially reasonable titers (>10.sup.7 Log TCID.sub.50/mL)
(FIG. 1 and data not shown). The genetic and antigenic
characteristics of virus grown in MDCK cells was compared to that
of virus grown in eggs. No significant changes in the genomic
sequence were seen (data not shown) and the antigenicity as
determined by HAI titers were comparable (Table 1).
Fluorescent Focus Assay: MDCK and Vero cells were grown in 96 well
black plates over 4 days (DMEM+4 mM glutamine+PEN/Strep). Each well
was infected with the ca/ts influenza B-strains (B/HongKong/330/01
and B/Yamanashi/166/98) at an MOI of .about.0.01 in DMEM+4 mM
glutamine+60 mU/mL TPCK trypsin. The virus infected plates were
fixed and immuno-stained as follows to determine the spread of
infection. The medium containing virus was removed from each plate
and the plates washed once with 200 .mu.l/well with DPBS (no
Ca2+/Mg2+) and the plates were then fixed by addition of 200
.mu.l/well of cold 4% (v/v) paraformaldehyde in PBS. The plates
were washed twice with 200 .mu.l/well of DPBS (no
Ca.sup.2+/Mg.sup.2+) followed by incubation of the cells with
primary antibody (sheep anti B yamanshi and sheep anti B hongkong
diluted in 0.1% saponin, 1% BSA in PBS at a ratio of 1:1000). After
incubation for an hour, the primary antibody was removed and cells
were washed thrice with 0.1% Tween 20 in PBS and the wells were
incubated with secondary antibody (rabbit anti sheep labeled with
FITC in 0.1% saponin, 1% BSA in PBS at 1:100 ratio dilution). The
wells were visualized daily for 4 days using a fluorescence
microscope and the images were taken daily using SPOT program.
Results And Discussion
A fluorescent focus assay was use to assess whether there was
spread of infection of ca/ts influenza B-strains in MDCK and Vero
and also assess if there was any difference in the spread of virus
infection among the 50 cell clones of Vero. Since the fluorescence
in the monolayer increased over 4 days in the MDCK cells but not in
the Vero cells (see, FIG. 1A), it was concluded that the Vero were
not permissive for the production of ca/ts B strains while MDCK
were. This data was similar to the data in earlier experiments that
showed that B-strains could be produced to 7-7.5 log.sub.10
TCID.sub.50 in MDCK cells but only to 4-4.5 log.sub.10 TCID.sub.50
in Vero Cells (data not shown).
The MDCK cells were also tested for their ability to support
replication of a number of ca/ts/att reassortant strains including
a potential pandemic vaccine strain, ca A/Vietnam/1203/2004. MDCK
cells were infected at a low multiplicity of infection with ca
A/Vietnam/1203/2004 and virus in the supernatant was quantified at
various times post infection. By 48 hours post infection, the
titers of ca A/Vietnam/1203/2004 reached approximately 8 log.sub.10
TCID.sub.50/mL and remained stable for the next 3 to 4 days. See
FIG. 1B and Table 2.
Ca/ts/att strains of type A/H1N1, A/H5N1, A/H3N2 and B replicated
to relatively high titers in MDCK cells. In addition, passaging
these ca/ts/att strains in MDCK cells did not significantly alter
their genomic sequence. Three ca/ts/att strains, ca A/Sydney/05/97,
ca A/Beijing/262/95, and ca B/Ann Arbor/1/94 were passaged once or
twice in MDCK cells and the entire coding regions of all 6 internal
genes were sequenced and compared to the starting material. No
nucleotide changes were observed (data not shown), demonstrating
that this passaging through this substrate did not change the
genetic composition of these strains. Further sequence
characterizations is performed on different vaccine strains
produced in MDCK cells under conditions that are expected to mimic
the production process including media composition, input dose
(moi), temperature of incubation and time of harvest. Based on the
preliminary data, it is expected that there will be no significant
changes in the genomic sequence of MDCK-produced virus.
Because the genome was genetically stable following passage in MDCK
cell, the biological traits of the vaccine produced in eggs or MDCK
cells are expected to be indistinguishable. However, the primary
viral product from cell culture may have some subtle differences
compared to the egg based product, particularly with respect to
post-translational modification of viral proteins including HA and
NA, or composition of lipids in the viral membrane; both of which
could potentially change the overall physical properties of the
virion. Preliminary preclinical data on the antigenicity of cell
culture produced and egg produced vaccine demonstrated that there
were no detectable differences in this important parameter. Egg
stocks of several vaccine strains were passaged through MDCK cells
and the antigenicity of both products was determined by measuring
the HAI titers using reference antisera. As show in Table 1, all
the HAI titers were within 2-fold of one another, indicating that
replication of the vaccine in cells did not change the antigenicity
of the vaccine compared to egg derived material.
TABLE-US-00001 TABLE 1 HAI Titers of strains produced in eggs and
MDCK cells HAI Titer Strain Egg derived MDCK derived A/Panama/20/99
256 256 A/Wuhan/359/95 1024 2048 A/Wyoming/03/2003 512 1024
B/Jilin/20/2003 64 32 B/Hong Kong/330/01 64 64 B/Jiangsu/10/2003
128 128
Example 2
Derivation of Non-Tumorigenic Serum MDCK Cells
MDCK cells have been traditionally used for the titration of
influenza viruses (Zambon, 1988, in Textbook of Influenza, ed
Nicholson, Webster and Hay, ch 24, pg 324-332, Blackwell Science)
and thus could be used for the propagation of influenza for the
production of vaccine materials. However, MDCK cells have
traditionally been grown in basal medium formulations like Eagle's
Minimal Essential Medium (EMEM) supplemented with FBS. Multiple
reports indicate that MDCK cells may be tumorigenic when cultivated
under these conditions and/or for extended periods of time (see for
example, Gaush et al., Proc Soc Exp Biol Med, 122:931; Leighton et
al., 1968, Science, 163:472 and Leighton et al., 1970, Cancer,
26:1022). Thus, there is concern about the use of MDCK cells for
the production of vaccine materials and efforts have focused on the
development of other cell lines (e.g., PER.C6 and VERO).
Unfortunately, not all influenza strains grow well in other
mammalian cell lines, in particular the cold adapted influenza
viruses that comprise FluMist.RTM., a live attenuated influenza
vaccine, only grow to reasonable titers (>10.sup.7 TCID 50/mL)
in MDCK cells (see Example 1, supra). Early reports characterizing
MDCK cells indicate that early passages of MDCK cells may not be
tumorigenic (Gaush et al., 1966, Proc Soc Exp Biol Med. 122:931).
It was the goal of this experiment to establish a culture media and
passage protocol to maintain MDCK cells in a non-tumorigenic
state.
MDCK cells obtained from the ATCC(CCL 34) were expanded in T-flasks
using DMEM supplemented with 10% FBS, 4 mM glutamine and 4.5 g/L
glucose as the growth medium. A pre-Master MDCK cell bank was
established on the serum grown MDCK cells (MDCK-S cells), which was
tested for bacterial/fungal contaminants and mycoplasma
contamination using routine tests performed by a commercial
contractor (BioReliance, Rockville, Md.). The cells were found to
be negative for the presence of bacterial/fungal contaminants. The
MDCK-S cells were also found to be negative for the presence of
cultivatable mycoplasma. The MDCK-S cells from the bank were also
tested by a karyotype assay and found to be canine in origin and
had a modal chromosome number of 78 with chromosome numbers ranging
from 70 to 84. The MDCK-S cells were then passaged for another 20
passages from a vial of PreMCB and tested for karyology and
tumorigenicity in an vivo adult nude mice model. The karyology test
showed that late passage MDCK-S cells (p 81/24) showed the same
modal chromosome number (78) and range of chromosomes (70 to 84) as
the early passage MDCK-S cells, showing that the cells did not
change on extended passaging. 1.times.10.sup.7 MDCK-S cells when
injected subcutaneously into adult nude mice did not result in the
formation of any nodules and were deemed to be non tumorigenic.
Materials and Methods
Materials: MDCK cell (ATCC, Cat. No: CCL-34); T-25, T-75, T-225
flasks (Corning, Cat No.: 430639, 430641, 431082); Dulbecco's
Modified Eagle's Medium (DMEM) powder (Gibco, Grand Island N.Y.,
Formulation No.: 01-5052EF); Fetal Bovine Serum, Gamma-irradiated
(JRH, Lenexa Kans., Cat. No.: 12107-500M); L-Glutamine (JRH, Lenexa
Kans., Cat. No.: 59202-100M); D-Glucose (Amresco, Cat. No.:
0188-1KG); Dulbecco's Phosphate buffered saline (DPBS) without
Ca.sup.2+ and Mg.sup.2+ powder (Gibco, Grand Island N.Y., Cat. No.:
21600-069); 0.05% Trypsin-EDTA (Gibco, Grand Island N.Y., Cat. No.:
25300) Dimethylsulphoxide, DMSO (Sigma, St. Louis Miss., Cat. No.:
D2650); 0.4% w/v Trypan blue dye in PBS (Sigma, St. Louis Miss.,
Cat. No.: T8154); CO.sub.2 Incubator (Form a Scientific, Model No.:
3110); YSI Bioanalyzer (YSI, Model No.: 2700 select); Vitro
Chemistry System (Ortho clinic, Model: DT60 II); Improved Neubaurr
hemacytometer (Hausser Scientific, Brightline 0.1 mm deep/Reichert,
Brightline 0.1 mm deep).
Subculturing of Serum MDCK (MDCK-S) cells in Tissue Culture Flasks:
A vial of serum MDCK cells was obtained from the ATCC. The cells
were grown in DMEM medium supplemented with 10% (v/v) FBS, 4.5 g/L
glucose, 2.2 g/L NaHCO.sub.3 and 4 mM L-glutamine in T-75 flasks.
The cells were passaged 3 or 4 days postseeding, with a complete
medium exchange performed on day 3 after seeding if the cells were
passaged on day 4. The cells were recovered from T-flasks as
described below.
The spent growth medium was removed and the cell monolayer washed
twice with DPBS (calcium and magnesium free). The appropriate
amount of trypsin-EDTA (3 mL/T-75, 7.5 mL/T-225), prewarmed in a
37.degree. C. water batch, was added to each flask and the T-flasks
incubated in a 37.degree. C., 5% CO.sub.2 incubator for about 15-20
min. The flasks were checked every 5 minutes to check if cells had
detached and the flasks were rapped several times to help detach
the cells. When the cells had completed detached from the T-flask,
the trypsin was inhibited by addition of equal volumes of complete
growth medium containing 10% serum (3 mL/T-75, 7.5 mL/T-225). The
cell suspension was aspirated up and down with an appropriately
sized pipette to break any large cell clumps. Two 0.5 mL samples of
cell suspension were counted in a hemacytometer. The cell counts
were repeated if the results of the two counts were not within 15%
of each other. The cells were diluted to 0.05.times.10.sup.6 viable
cells/mL in fresh warm growth medium (DMEM+10% FBS+4.5 g/L
glucose+4 mM glutamine) in fresh flasks and seeded in T-flasks (35
mL/T75 or 100 mL/T-225). The flasks were then incubated in a
37.+-.1.degree. C., 5% CO.sub.2 environment for 3 days prior to
subculturing or media exchange.
Preparation of MDCK-S cell bank: MDCK-S cells were expanded in
T-flasks as described above until the total required amount of
cells needed for banking could be recovered (4.times.10.sup.6
cells/vial.times.number of vials). The MDCK-S cells were recovered
when in the exponential growth phase (3 days post seeding) by
trypsinization as described. The MDCK-S cell suspensions from
individual flasks were pooled and cells were recovered by
centrifugation at 150-250 g for 7.+-.1 min. The supernatant was
aspirated off from each tube and the cell pellets were resuspended
in fresh complete growth medium (DMEM+10% FBS+4.5 g/L glucose+4 mM
glutamine). The cell suspensions from different centrifuge bottles
were pooled and cell suspension was aspirated up and down with a
pipette several times to break any large cells clumps. The total
cell number was determined and the total number of vials that could
be frozen at 4.times.10.sup.6 cells/vial was determined.
The volume of cell suspension was then adjusted to the above value
using fresh growth medium. Equal volumes of freshly prepared
2.times. freezing medium (DMEM+10% FBS+4 mM glutamine+4.5/L
glucose+15% DMSO) was added to the cell suspension. Cell suspension
was mixed thoroughly and 1 mL of cell suspension was dispensed into
each cryovial. All the vials were transferred into Nalgene freezing
containers and were placed in a .ltoreq.-60.degree. C. freezer. The
frozen vials were transferred to a liquid nitrogen storage
tank.
Preparation of MDCK-S cells Growth Curve in T-75 flasks: Cells were
passaged at least 4 times (post thaw) in their growth medium prior
to cell growth curve study. MDCK-S cells were expanded into T-225
flasks in order to obtain at least 2.7.times.10.sup.7 total cells.
The flasks were grown to 80-95% confluent prior to trypsinization
as described above. The recovered MDCK-S cells were pooled and cell
suspension aspirated up and down with a pipette several times to
break any large cell clumps. Two samples (0.5 mL) were removed for
cell counts and cell density determined. The two sample counts were
repeated if they were not within 15% of each other.
2.7.times.10.sup.7 total MDCK-S cells were then diluted to a total
volume of 540 mL of complete growth medium (5.0.times.10.sup.4
cells/mL). This MDCK-S cell suspension was then dispensed into
14.times.T-75 flasks (35 mL/T-75 flask). The flasks were placed in
a 37.+-.1.degree. C., 5% CO.sub.2 incubator.
Two T-flasks were removed daily from incubator for cell counts and
metabolic analysis. Two samples (approximately 1.0 mL) of cell
culture media were removed from each flask for metabolic analysis.
One sample was used to determine glucose, lactate, glutamine,
glutamate and ammonia concentrations using the YSI and Vitros
analyzers. The other sample was frozen at -70.degree. C. for amino
acid analysis at a later date. The MDCK-S cells were recovered from
each flask by trypsinization as described above. The cell density
was determined and the total number of cells/T-flask was also
determined. The two counts were repeated if they were not within
15% of each other. The numbers presented are the average of two
independent growth curves studies performed at two different
passage numbers (p63 and p65) of MDCK-S cells.
Karyology Test: The karyology test was carried out at Applied
Genetics Laboratories in Melbourne, Fla. Briefly, MDCK-S cells
grown in T-225 flasks were shipped to Applied Genetics
Laboratories. The cells were maintained and subcultured as per the
methods listed above. When the cells were thought to have enough
mitotic cells, the cells were harvested for mitotic analysis. The
cells were treated with colcemid (0.02 .mu.g/mL) for 150 minutes at
37.degree. C. The cells were then harvested by trypsinization, and
cells centrifuged for 5 minutes at 200 g. The supernatant was
aspirated off and the cells resuspended in prewarmed hypotonic
solution and incubated at 37.degree. C. for 10 minutes. The swollen
cells were pelleted by centrifugation and then fixed by incubation
in carnoy's solution (3:1 methanol:glacial acetic acid) at room
temperature for 40 minutes. The cells were again centrifuged and
cells washed at least twice with Carnoy's fixative. After the last
centrifugation, the cells were resuspended in 1 to 3 ml of fresh
fixative to produce an opalescent cell suspension. Drops of the
final cell suspension were placed on clean slides and air
dried.
Cells were stained by addition of Wright's stain solution in
phosphate buffer to the slides and incubating for 7-10 minutes. The
slides were washed with tap water after 7-10 minutes and then air
dried. The cells were scanned with low power objectives (10.times.)
to find cells in the metaphase stage of cell division and the
chromosomes of cells in metaphase were analyzed via a high power
oil immersion lens (100.times.). A 100 cells in metaphase were
analyzed for cytogenic abnormalities and chromosome count. 1000
cells were scanned to determine polyploid frequency and mitotic
index (percent of cells under going mitosis).
Sterility Testing of the MDCK-S PRE-MCB (Bacteriostatic and
Fungastatic and Four Media Sterility): The MDCK-S Pre-MCB was
tested for bacteriostatic and funstatic activity at Bioreliance
Inc., Rockville, Md. The assay was performed to meet US 26 and 21
CFR 610.12 requirements. This assays tests whether the there is a
difference in growth of control organisms (Bacillus subtilis,
Candida albicans, Clostridium sporogenes, Staphylococcus aureus,
Pseudomonas aeruginonsa, Aspergillus Niger) inoculated in
appropriate broth medium containing 0.1 mL of test sample versus
broth medium containing control organisms only. Briefly, the test
article was inoculated into three tubes of TSB (soybean-casein
digest medium), four tubes of THIO (fluid thioglycollate medium),
two tubes of SAB (Sabourand Dextrose Agar) and one tube of PYG
(peptone yeast extract). Each control organism containing less that
100 cfu of control organism was then inoculated into the
appropriate media type. Positive controls consisted of Bacillus
subtilis in TSB and THIO, Candida albicans in TSB and SAB (at
20-25.degree. C. and 30-35.degree. C.), Clostridium sporogenes in
THIO and PYG, Pseudomonas aeruginosa, Staphyloccus aureus and
Aspergillus niger. The negative control was sterile PBS. The media
were incubated for 3-5 days and checked for growth of
organisms.
The test article was also analyzed for presence of bacterial and
fungal contaminants using the four media sterility test at
Bioreliance, Rockville Md. and the assay was designed to meet USP
26, EP and 21CFR610.12 requirements. Briefly, the test article was
inoculated in two tubes of two tubes of TSB (soybean-casein digest
medium), two tubes of THIO (fluid thioglycollate medium), three
tubes of SAB (Sabourand Dextrose Agar) and two tubes of PYG
(peptone yeast extract). The media were incubated at appropriate
temperatures (SAB slants were incubated at two temperatures) and
all tubes observed over a 14 day period with the tubes checked on
third/fourth or fifth day, seventh or eight day and fourteenth day
of testing. Any test article inoculated tubes which appeared turbid
were plated out and gram stains performed on the plate. Negative
controls were sterile PBS.
Mycoplasma/mycoplasmstasis test: A vial of frozen MDCK-S cells
(MDCK preMCB lot no. 747p105) was sent to Bioreliance. The cells
were expanded and cultured in T-flasks as explained above. Cell
lysates at a concentration of 5.times.10.sup.5 cells/mL were
prepared and frozen at -70.degree. C. The test article was tested
for ability to inhibit growth of Mycoplasmapneumoniae, Mycoplasma
orale and Mycoplasma hyorhinis either in agar broth/plates and/or
in VERO cells.
For the agar isolation assay, the test article was test either
spiked or unspiked on agar plates or broth bottles. The test
article was spiked with Mycoplasmapneumoniae and Mycoplasma orale
to achieve a dilution of 10 to 100 cfu/0.2 mL (for Agar test) and
10 to 100 cfu/10 mL (for semi broth assay). A portion of the test
sample was not spiked. 4 semi solid broth bottles were inoculated
with 10 ml each of spiked (2 bottles) or unspiked (2 bottles). One
bottle each of spiked/upspiked were incubated either aerobically or
anaerobically at appropriate temperatures. 10 type A agar plates
and 10 type B agar plates were inoculated with each spiked sample
or unspiked sample. Half the type A agar plates and type B agar
plates were incubated either aerobically or anaerobically at
appropriate temperatures. Uninoculated mycoplasma semi-solid broth
served as the uninoculated negative control. All broth bottles were
observed for 21 days. Each broth bottle (with exception of
uninoculated negative control) was subcultured on days 3, 7 and 14
onto Type A agar plates or Type B agar plates (10 plates each, 0.2
mL/plate) and incubated under the same conditions as the
appropriate bottle. They were examined once a day for 21 days.
For the enhanced VERO cell culture assay, the test article was
tested spiked or unspiked. The test article was spiked with M.
orale and M. hyorhinis at a concentration of 10-100 cfu/0.2 mL. The
spiked test articles, unspiked test articles, positive controls and
negative controls were each inoculated onto T-75 flasks of VERO
cell cultures. After 3-5 days of incubation, the cells from each
flask were scraped and snap frozen. Two tenths of one mL of cell
lysate from each flask, was inoculated into each of well of a six
well plate containing VERO cells. In addition positive and negative
controls were inoculated into appropriate wells of six well plates
containing VERO cells. After 3-5 days the cells were fixed and
stained with DNA binding HOECHT dye and evaluated for presence of
mycoplasma.
Tumorizenicity test of MDCK-S cells in Nude Mice: Evaluation of
tumor formation in nude (nu/nu) athymic mice was performed by
BioReliance.RTM., Rockville, Md. Briefly, thirty female athymic
mice (4 weeks old) were injected subcutaneously with 0.2 mL
(1.times.10.sup.7 cells/mice) of either positive control (18Cl-10T
cells), negative control (Syrian hamster embryo cells; SHE cells)
or the test cells (Serum MDCK cells, 747p105 high passage). The
animals were randomized before injection and all mice were injected
using a 22 gauge needle on the same day. All animals were observed
every working day and the injection site was palpated twice a week
for lesion development for a period of eighty four days. Each
lesion was measured and the animals were held as long as there was
no visible increase in size of the lesion. This was for a maximum
of 3 months. All mice were sacrificed and necropsied after 84 days
and the injection site, lungs, scapular lymph nodes and gross
lesions analyzed by histopathological methods.
Replication of cold adapted influenza strains in MDCK-S: T-75
flasks were seeded at 5.times.10.sup.4 cells/mL (35 mL of DMEM+10%
FBS+4 mM glutamine) and grown in an incubator maintained at
37.degree. C. and 5% CO.sub.2 for 3 days. 3 days post seeding, the
total cells per T-flask were determined by harvesting using trypsin
EDTA and cell counts determined by Trypan-Blue Exclusion. The
remaining T-flasks were then infected as follows. The growth media
was aspirated off and cells washed twice with 10 mL DPBS (no
Ca.sup.2+/Mg.sup.2+) per flask. The amount of virus to infect each
T-flask at a multiplicity of infection (MOI) of 0.01 was determined
as per the equation below:
.times..times..times..times..times..function..times..times..times..times.-
.times..times..times..times..times..times..times. ##EQU00001##
MOI being defined as the virus particles per cell added
The required amount of virus is then added to 35 mL of post
infection medium in each T-flask. (DMEM+4 mM glutamine+60 mu/mL
TPCK trypsin). The T-flasks were then incubated at 33.degree. C.,
5% CO.sub.2 and samples taken each day for 6 days. 10.times.SP was
added to each sample as a stabilizer and the samples were stored at
<-70.degree. C. prior to testing for infectivity.
The concentration of virus present in each sample was determined
according to a median tissue culture infectious dose (TCID.sub.50)
assay that measures infectious virions. Briefly, MDCK cells were
grown to confluent monolayers in 96-well microtiter plates and a
serial dilutions of calts influenza virus sample was added. The
samples in the MDCK cell assay plate were typically at a final
dilution of 10.sup.-4 to 10.sup.-10. The wells in columns 1-5 and
8-12 contained virus-diluted sample and wells in columns 6-7
received only virus diluent and served as cell controls. This
format produced two data points (n=2) per plate. Replication of
virus in the MDCK cells resulted in cell death and the release of
progeny virus into the culture supernatant. The progeny virus
infected other cells, resulting in the eventual destruction of the
monolayer. The cytopathic effect (CPE) resulting from infection was
allowed to develop during an incubation at 33.+-.1.degree. C. in a
CO.sub.2 environment for a period of six days. The plates were then
removed from the incubator, the media in the wells discarded, and
100 .mu.l of MEM+4 mM glutamine+penicillin/streptomycin+MTT was
added to each well. The plates were incubated for 6 hrs at
37.degree. C. 5% CO.sub.2 and the number of wells showing CPE was
determined by visual inspection of the color formed in each well
(yellow/orange signifies CPE wells and solid purple signifying no
CPE). The number of wells showing CPE in each half plate was used
to calculate the titer (log.sub.10 TCID.sub.50/mL) based on the
Karber modification of the Reed-Muench method.
Results and Discussion
Two frozen vials of serum MDCK cells were thawed in complete growth
medium (DMEM+10% FBS+4 mM glutamine+4.5 g/L glucose) on separate
occasions into T-75 flasks. The cell viability on thaw was 97% and
98% respectively. Cells achieved confluence three days after
thawing. The morphology of cells were epithelial-like and similar
to the stock obtained from ATCC (FIG. 3). These cells were passaged
5 times and a Pre-master cell bank PreMCB was established for these
serum grown MDCK cells (MDCK-S cells). FIG. 2 outlines the process
used for the derivation of the MDCK-S pre-master cell bank
(pre-MCB).
The growth curves for MDCK-S cells in 10% FBS DMEM medium are
showed in FIG. 4. The results are the average of two experiments
using cells at different passage numbers (P63&P65). MDCK-S
cells had an approximately 1 day lag phase where the cell number
did not double from seeding (1.75.times.10.sup.6 total cell/T75
flask at seeding and 2.9.times.10.sup.6 total/T-75 day 1). The
glucose consumption/lactate production rate was almost zero for the
first day showing that the cells were in the lag phase (FIG. 5).
Then cells grew exponentially during cell growth period before
entering stationary phase at day 4 post seeding. The doubling time
of MCDK-S cells in exponential growth phase was 23.1 hours. During
the exponential phase the glucose consumption and lactate
production mirrored each other with lactate increasing in
concentration as the glucose concentration decreased (FIG. 5). The
glucose consumption/lactate production rate correlated well with
the cell growth curve (compare FIGS. 4 and 5). The rates were low
during lag phase, increased to 2.93 mM/day for glucose, 3.43 mM/day
for lactate during the exponential phase from day 1 to day 4.
The MDCK-S cells entered into the stationary phase day 4 post
seeding, and achieved a maximum cell density was around
29.+-.0.99.+-.10.sup.6 cell on day 5 post seeding (FIG. 4). The
cell number remained constant after reaching maximum density and up
to day 7 in this study. The glucose consumption and lactate
production rate slowed to 0.33 mM/day for glucose and 0.25 mM/day
for lactate in stationary phase. There was still approximately 12
mM glucose remaining in the medium after 7 days culture. The ratio
of amount of glucose consumed to lactate produced at day 4 was
1.2.
Glutamine consumption and both glutamate and ammonia production of
the MDCK-S cells are shown in FIG. 6. The rate of glutamine
consumption and production of ammonia correlated with the cell
growth curve as well (compare FIGS. 4 and 6). The MDCK-S cells
consumed glutamine at a rate of 0.49 mM/day during the exponential
growth phase up to day 4 while producing ammonia at a rate of 0.32
mM/day up to day 5. Then the rate of glutamine consumption dropped
to 0.24 mM/day while the ammonia production rate dropped to 0.11
mM/day, when the cells entered the stationary phase. The ratio of
ammonia production to glutamine consumption was 0.7 on day 4 post
seeding. Glutamate generated from glutamine metabolism did not
accumulate in this 7 days cell growth study.
The karyology of the MDCK-S cells was tested at passage 61/4 and
passage 81/24. The G-band chromosome analysis showed that the cells
were canine in origin. The distributions of chromosome number in
100 metaphases cells are shown in FIG. 7. The chromosome count
ranged from 70 to 84 chromosomes per metaphase for cells at low
passage 61/4 and 70 to 84 chromosomes for high passage 81/24. Both
passages had a modal chromosome number of 78 chromosomes. The
distribution of chromosomes did not change with passaging. The
modality of cells were as expected for a normal canine kidney cell
(Starke et al., 1972, Prog Immunobiol Stand., 5:178).
The MDCK-S preMCB was tested for presence any bacterial, fungal or
mycoplasma contaminants. The pre-MCB was passed sterility test
(four media sterility test using direct inoculation method to check
bacterial and fungal contaminants) and was found to be negative for
presence of mycoplasma (agar-cultivable and non-agar cultivable
assay). The test article was also found not to inhibit the growth
of positive controls in both the bacteriostasis/fungistatis test
and mycoplasmstatis test.
MDCK-S cells at passage 81/24 (pre-MCB+20 passages) were put on
nude mice for tumorigenicity test for 3 months. No neoplasma were
diagnosed in any mice that were inoculated with MDCK-S cells
demonstrating that MDCK-S cells were not tumorigenic (Table 4).
The MDCK-S cells were tested and found to be capable of supporting
the replication of cold adapted temperature sensitive attenuated
reassortant influenza strains (Table 2).
TABLE-US-00002 TABLE 2 Growth of cold adapted influenza virus
strains in serum and serum-free MediV SF101 adapted MDCK cells
Virus Strain Serum MDCK Serum-free MDCK (6:2 reassortant)
(log.sub.10 TCID.sub.50/mL) (log.sub.10 TCID.sub.50/mL) A/New
Caledonia/20/99 8.1 7.8 A/Texas/36/91 6.4 <5.2 A/Panama/2007/99
6.8 6.4 A/Sydney/05/97 7.0 6.5 B/Brisbane/32/2002 7.2 7.5
B/HongKong/330/01 7.2 7.4 B/Victoria/504/2000 6.9 7.5
Example 3
Derivation of Serum-Free MDCK Cells in Taub's Media
The results detailed Example 2 above demonstrate that MDCK cells
can be cultivated under conditions that maintain their epithelial
morphology and normal karyology as well as their ability to
replicate cold adapted influenza strains. In addition, we
demonstrated that cultivation of MDCK cells under the conditions
developed in the above study results in MDCK cells that are
non-tumorigenic. However, the culture medium used in Example 2
contains fetal bovine serum (FBS). FBS is a complex mixture of
constituents and there have been problems reported of lot-to-lot
variation. Also, the ongoing problems with bovine spongiform
encephalopathy (BSE) in cows raise safety concerns. The development
of serum-free medium in which the non-tumorigenic nature and growth
characteristics of the MDCK-S cell line is maintained is important
for increasing the safety of biologicals produced for therapy and
vaccination.
Madin Darby Canine Kidney Cells (MDCK) cells obtained from the ATCC
(ccl 34) were expanded in T-flasks using DMEM supplemented with 10%
FBS, 4 mM glutamine and 4.5 g/L glucose as the growth medium for 5
passages. The cells were then transferred to serum-free Taub's
media (see below for formulation). The cells adapted to grow in the
Taub's media formulations were designated MDCK-T. A pre-MCB was
established for the MDCK-T cells (see FIG. 8) and was tested for
bacterial/fungal contaminants and mycoplasma contamination. The
cells the MDCK-T cell pre-Master cell bank were also tested by a
karyotype assay found to be canine in origin and had a modal
chromosome number of 78 with chromosome numbers ranging from 52 to
84. In addition, the MDCK-T cells were passaged for at least
another 20 passages from a vial of PreMCB and tested for karyology
and tumorigenicity in an vivo adult nude mice model. However, the
MDCK-T cells were found to be tumorigenic in this model indicating
that the published Taub's media did not support the stable
cultivation of MDCK cells for the production of human vaccine
material.
Materials and Methods
Materials: MDCK cell (ATCC, Cat. No: CCL-34, passage 54); T-25,
T-75, T-225 flasks (Corning, Cat No.: 430639, 430641, 431082);
Dulbecco's Modified Eagle's Medium (DMEM) powder (Gibco, Grand
Island N.Y., Formulation No.: 01-5052EF); Ham F12 Nutrients mixture
powder (Gibco, Grand Island N.Y., Cat. No.: 21700-075); Fetal
Bovine Serum, Gamma-irradiated (JRH, Lenexa Kans., Cat. No.:
12107-500M); L-Glutamine (JRH, Lenexa Kans., Cat. No.: 59202-100M);
D-Glucose (Amresco, Cat. No.: 0188-1KG); Dulbecco's Phosphate
buffered saline (DPBS) without Ca.sup.2+ and Mg.sup.2+ powder
(Gibco, Grand Island N.Y., Cat. No.: 21600-069); Insulin powder
(Serological, Cat. No. 4506); Transferrin (APO form) (Gibco, Grand
Island N.Y., Cat. No.: 11108-016); Prostaglandin E1 (Sigma, St.
Louis Miss., Cat. No.: P7527); Hydrocortisone (Mallinckrodt, Cat.
No.: 8830(-05)); Triidothyronine (Sigma, St. Louis Miss., Cat. No.:
T5516); Sodium Selenium (EMD, Cat. No.: 6607-31); 0.05%
Trypsin-EDTA (Gibco, Grand Island N.Y., Cat. No.: 25300); Lima bean
trypsin inhibitor (Worthington, Cat. No.:LS002829);
Dimethylsulphoxide, DMSO (Sigma, St. Louis Miss., Cat. No.: D2650);
0.4% w/v Trypan blue dye in PBS (Sigma, St. Louis Miss., Cat. No.:
T8154); Improved Neubaurr hemacytometer (Hausser Scientific,
Brightline 0.1 mm deep/Reichert, Brightline 0.1 mm deep); YSI
Bioanalyzer (YSI, Model No.: 2700 select); Vitro Chemistry System
(Ortho clinic, Model: DT60 II).
Formulation of Taub's Serum-free Media: Taub's media (Taub and
Livingston, 1981, Ann NY Acad. Sci., 372:406) is a serum-free media
formulation that consists of DMEM/HAM F12 (1:1) containing 4.5 g/L
glucose and 4 mM glutamine as the basal media formulation, to which
the hormones/factors are added as indicated in Table 3.
TABLE-US-00003 TABLE 3 Hormones and growth factors added to
serum-free media formulations Name of Component Final Concentration
Insulin 5 .mu.g/mL Transferrin 5 .mu.g/mL Triiodothyronine
(T.sub.3) 5 .times. 10.sup.-12 M Hydrocortisone 5 .times. 10.sup.-8
M Prostaglandin E.sub.1 25 ng/mL Sodium Selenite 10.sup.-8 M
Taub's SFM is made fresh at the time of passaging or refeed by the
addition of stock solutions of hormone supplements to SF DMEM/Ham
F12 medium+4 mM glutamine+4.5 g/L glucose+10.sup.-8 M sodium
selenite. 100 mL of Taubs Media is made by addition of 100 .mu.L of
insulin stock (5 mg/mL) solution, 100 .mu.L transferrin stock
solution (5 mg/mL), 100 .mu.L triiodothyronine (T3) stock solution
(5.times.10.sup.-9 M), 5 .mu.L of hydrocortisone stock solution
(10.sup.-3 M) and 50 .mu.L of prostaglandin E1 stock solution (50
.mu.g/mL) to basal DMEM/Ham F12 medium+4 mM glutamine+4.5 g/L
glucose+10.sup.-8 M sodium selenite. All stocks solutions are
prepared as follows: Insulin Stock Solution--A 5 mg/ml stock
solution is made by dissolving the appropriate amount of insulin in
0.01 N HCl. The solution is passed through a 0.2 micron sterilizing
grade filter and aliquoted into Nalgene cryovial and stored at
4.degree. C. Transferrin Stock Solution--A 5 mg/ml stock solution
is made by dissolving the appropriate amount of transferrin in
MilliQ water. The solution is passed through a sterilizing grade
filter and then aliquoted into Nalgene cryovial and store
<-20.degree. C. Triiodothyronine (T.sub.3) Stock Solution--A
stock solution is made by dissolving the appropriate amount of T3
in 0.02 N NaOH to obtain a 10.sup.-4 M solution. This is stock
solution is further diluted to a concentration of 5.times.10.sup.-9
M stock solution with 0.02 N NaOH, passed through a sterilizing
grade filter, aliquoted into Nalgene cryovial and stored at
<-20.degree. C. Hydrocortisone Stock Solution--A 10.sup.-3 M
stock solution is made by dissolving the appropriate amount of
hydrocortisone in 100% EtOH and aliquoted into Nalgene cryovials.
The vials are stored at 4.degree. C. for 3-4 months. Prostaglandin
E.sub.1 Stock Solution--A 50 .mu.g/mL stock solution made by
dissolving the appropriate amount of PGE1 in 100% sterile EtOH and
aliquoted into Nalgene cryovial and stored at <-20.degree. C.
Na.sub.2SeO.sub.3 Stock Solution--A 10.sup.-2 M stock solution is
made by dissolving the appropriate amount of sodium selenide in WFI
water or MilliQ water. This is further diluted in water to a final
concentration of 10.sup.-5 M passed through a sterilizing grade
filter and stored at 4.degree. C.
Adaptation of MDCK-S cells into Serum-free Taub's media: A frozen
vial of MDCK cells from ATCC (passage 54) was grown in 10% FBS DMEM
medium with 4.5 g/L glucose, 2.2 g/L NaHCO.sub.3 and 4 mM
L-glutamine for 5 passages (as described above) before passaging
into a serum-free Taub's media. Serum MDCK grown in a T-75 flask
were recovered by trypsinization. The spent growth medium was
removed and cell monolayer washed twice with DPBS (calcium and
magnesium free) and then DPBS was discarded. The appropriate amount
of pre-warmed trypsin-EDTA (3 mL/T-75) was added and the T-flask
was incubated in a 37.degree. C., 5% CO.sub.2 incubator for about
15 min. The flasks were rapped against the palm of the hand several
times to completely detach the cells. Equal volume of lima bean
trypsin inhibitor was added to neutralize the trypsin and two
samples were taken to determine concentration of cells in the cell
suspension. 1.75.times.10.sup.6 cells were then diluted into 35 mL
Taub's media in a fresh T75 flask. The flask was placed in an cell
culture incubator maintained at 5% CO.sub.2, 37.+-.1.degree. C. The
cells were either subcultured 3 days post seeding or a complete
medium exchange was performed on day 3 followed by subculturing on
day 4 postseeding.
Subculturing of Taub's media Adapted MDCK cells: The spent growth
medium was removed and cell monolayer washed twice with DPBS
(calcium and magnesium free). The appropriate amount of pre-warmed
trypsin-EDTA (3 mL/T-75, 7.5 mL/T-225) was added and the T-flask
was incubated in a 37.degree. C., 5% CO.sub.2 incubator for about
15 min. The flasks were rapped against the palm of the hand several
times to completely detach the cells. The trypsin was then
inhibited by addition of equal volumes of lima bean trypsin
inhibitor (3 mL/T-75, 7.5 mL/T-225). The cell suspension was
homogenized by aspirating up and down with an appropriately sized
pipette. Two 0.5 mL samples of cell suspension were taken for cell
counting. The cell counts were repeated if the results of the two
counts were not within 15% of each other. After counting, the cells
were diluted to 0.05.times.10.sup.6 viable cells/mL in fresh
prewarmed Taub's media in fresh flasks, for a total volume of 35
mL/T75 or 100 mL/T-225. The flasks were then incubated in a
37.+-.1.degree. C., 5% CO.sub.2 environment. Cells were either
subcultured to new T-flasks on day 3 (as described below) or a
complete media exchange was performed and the culture subcultured
to new T-flasks on day 4 post seeding.
Preparation of Taub's media Adapted MDCK cell PreMCB Banks: The
pre-master cell banks for the Taub's serum-free adapted MDCK cell
line (MDCK-T) were prepared as described in Example 2 above, except
that the 2.times. freezing medium was Taub's media+15% DMSO.
Characterization of Taub's media Adapted MDCK (MDCK-T) cells:
Karyology, sterility and mycoplasma testing of the MDCK-T preMCB
was performed as described in Example 2 except that Taub's media
was used in place of serum containing complete media. In addition
the growth curve characteristics of MDCK-T cells in T-75 flasks and
the replication of cold adapted influenza strains in MDCK-T cells
were examined as described in Example 2 except that Taub's media
was used in place of serum containing complete media.
Tumorigenicity studies were performed on MDCK-T cells at passage
88/29 (pre-MCB+20 passages) by BioReliance as described in Example
2 above.
Results and Discussion
A frozen vial of MDCK-T preMCB (passage 64/5) cells was thawed into
serum-free Taub's media in T-75 flasks. The cell viability was 97%
and 5.25.times.10.sup.6 cells were recovered from frozen vial upon
thawing. Cells were confluent three days after thawing. Cell
morphology showed epithelia-like cells similar to the parent MDCK-S
cells. (FIG. 9).
The growth curves for MDCK-T cells in Taub's SF medium are showed
in FIG. 10. The results are the average of two experiments using
cells at different passage numbers (P71/12 & P73/14). MDCK-T
cells had no lag phase with cells doubling one day post seeding
(3.42.times.10.sup.6 total cell/T75 flask day 1 versus
1.75.times.10.sup.6 total cell/T75 flask on day 0). The cells were
in the exponential phase of growth till day 4, when they entered
into the stationary phase. The doubling time of cells in the
exponential phase was 20.4 hrs. During the exponential phase (day 0
to day 4) they utilized glucose and glutamine (FIGS. 11 and 12)
while producing lactate and ammonia. The glucose
consumption/lactate production rate correlated well with the cell
growth curve (compare FIGS. 10 and 11). The glucose consumption
rate was 1.78 mM/day during the exponential phase from day 0 to day
4 and lactate was produced at a rate of 2.88 mM/day. MDCK-T cells
only consumed about a total of 10 mM glucose in the medium up to 7
days culture. The ratio of amount of glucose consumed to lactate
produced at day 4 post seeding was 1.2. The rate of glucose
consumption and lactate production slowed down after day 4 when
cells entered into the stationary phase, with the glucose
consumption being 0.65 mM/day and lactate being produced at a rate
of 0.46 mM/day. The maximum cell density of
37.+-.0.24.times.10.sup.6 was achieved around day 4 post seeding.
The cell density did not drop during the stationary phase and
remained constant till day 7.
The glutamine consumption rate and ammonia production rate were
similar to the MDCK-T cell growth and glucose/lactate profiles
(compare FIGS. 10, 11 and 12). The MDCK-T cells consumed glutamine
at a rate of 0.36 mM/day during the exponential growth phase (day 0
to day 4) with the rate dropping to 0.27 mM/day when the cells
entered the stationary phase (day 4 to day 7). Ammonia production
increased linearly up to day 7 at rate of 0.22 mM/day. The ratio of
ammonia production to glutamine consumption was 0.49 on day 4 post
seeding. Glutamate concentration did not change appreciably during
the entire 7 day period.
MDCK-T cells were tested for their ability to support ca/ts
influenza replication as per example 2. The results shown in Table
2 indicate that MDCK-T cells were able to support the replication
of ca/ts influenza replications to levels nearly the same as seen
for the MDCK-S cells.
MDCK-T cell karyology was tested at passage 68/9 and passage 88/29.
The G-band chromosome analysis showed that the cells were canine in
origin. The distributions of chromosome number in 100 metaphases
cells were shown in FIG. 13. The chromosome count ranged from 52 to
82 chromosomes per metaphase for cells at low passage 68/9, range
from 54 to 82 chromosomes for high passage 81/24 indicating that
the distribution of chromosomes did not change with passaging.
However, it can be seen that the MDCK-T cells show a wider spread
in chromosome number (52 to 84) as compared to the MDCK-S cells
(70-84).
The MDCK-T preMCB was tested for presence any bacterial, fungal or
mycoplasma contaminants. The MDCK-T pre-MCB was passed sterility
test (four media sterility test using direct inoculation method to
check bacterial and fungal contaminants) and was found to be
negative for presence of mycoplasma (agar-cultivable and non-agar
cultivable assay). The test article was also found not to inhibit
the growth of positive controls in both the
bacteriostasis/fungistatis test and mycoplasmstatis test.
MDCK-T cells at passage 88/29 (pre-MCB+20 passages) were put on
nude mice for tumorigenicity test for 3 months. The test article
was diagnosed as adenocarcinomas at the site of injection in six of
ten test article mice. This shows that the MDCK cells grown in SF
Taubs media are tumorigenic. The tumorigenicity, estimated TP50 and
karyology for MDCK-S and MDCK-T cells is summarized in Table 4
below.
Example 4
Derivation of Serum-Free MDCK Cells in MediV Serum-Free Medias:
The results detailed in Example 3 demonstrate that, although MDCK
cells adapted to grow in serum-free Taub's media (MDCK-T) had
excellent growth characteristics and were able to support the
replication of ca/ts influenza strains, they were tumorigenic.
Thus, these results indicate that MDCK cells can readily become
transformed in the standard serum-free media formulations reported
in the literature. In accordance with the invention, several
additional serum-free media formulations were developed and tested
for their ability to maintain the non-tumorigenic nature of the
MDCK-S cells. MDCK-S cells were adapted to each of the new
serum-free formulations designated MediV SFM 101, 102 and 103.
These serum-free adapted cell lines were designated MDCK-SF101,
-SF102 and -SF103, respectively and are referred to as "MDCK-SF",
collectively. PreMCBs were generated for each MDCK-SF adapted cell
line. The MDCK-SF cell line preMCBs were tested for
bacterial/fungal contaminants and mycoplasma contamination
(awaiting final results). The MDCK-SF preMCBs were also tested by a
karyotype assay, MDCK-SF101 and MDCK-SF102 cells had a modal
chromosome number of 78 with chromosome numbers ranging from and 70
to 82 and 60 to 80, respectively. In addition, the cells from each
serum-free media bank were passaged for at least another 20
passages from a vial of PreMCB and MDCK-SF103 was tested for
karyology and tumorigenicity in an vivo adult nude mice model. At
passage 87 MDCK-SF103 was found to have a modal chromosome number
of 78 ranging from 66 to 80 and were deemed to be non
tumorigenic.
Materials: MDCK cell (ATCC, Cat. No: CCL-34, passage 54); T-25,
T-75, T-225 flasks (Corning, Cat No.: 430639, 430641, 431082);
Dulbecco's Modified Eagle's Medium (DMEM) powder (Gibco, Grand
Island N.Y., Formulation No.: 01-5052EF); Ham F12 Nutrients mixture
powder (Gibco, Grand Island N.Y., Cat. No.: 21700-075); Fetal
Bovine Serum, Gamma-irradiated (JRH, Lenexa Kans., Cat. No.:
12107-500M); L-Glutamine (JRH, Lenexa Kans., Cat. No.: 59202-100M);
D-Glucose (Amresco, Cat. No.: 0188-1KG); Dulbecco's Phosphate
buffered saline (DPBS) without Ca.sup.2+ and Mg.sup.2+ powder
(Gibco, Grand Island N.Y., Cat. No.: 21600-069); Insulin powder
(Serological, Cat. No. 4506); Transferrin (APO form) (Gibco, Grand
Island N.Y., Cat. No.: 11108-016); Prostaglandin E1 (Sigma, St.
Louis Miss., Cat. No.: P7527); Hydrocortisone (Mallinckrodt, Cat.
No.: 8830(-05)); Triidothyronine (Sigma, St. Louis Miss., Cat. No.:
T5516); Sodium Selenium (EMD, Cat. No.: 6607-31); 0.05%
Trypsin-EDTA (Gibco, Grand Island N.Y., Cat. No.: 25300); Lima bean
trypsin inhibitor (Worthington, Cat. No.:LS002829);
Dimethylsulphoxide, DMSO (Sigma, St. Louis Miss., Cat. No.: D2650);
0.4% w/v Trypan blue dye in PBS (Sigma, St. Louis Miss., Cat. No.:
T8154); Improved Neubaurr hemacytometer (Hausser Scientific,
Brightline 0.1 mm deep/Reichert, Brightline 0.1 mm deep); YSI
Bioanalyzer (YSI, Model No.: 2700 select); Vitro Chemistry System
(Ortho clinic, Model: DT60 II).
Formulation of MediVSerum-free Medias (MediVSFM 101, 102 and 103):
Each MediV serum-free media formulation uses Taub's media (see the
methods section of example 2 above) as a basal media and adds
supplements as follows: MediV SFM 101: Taub's+2.5 g/L Wheat Peptone
E1 from Organo Techine (cat no 19559). Wheat Peptone E1 is stored
in water as a sterile 250 g/L stock solution. MediV SFM 102:
Taub's+100.times. chemically defined lipid concentrate from GIBCO
BRL (cat no. 11905) added to a final concentration of 1X. MediV SFM
103: Taub's+1.times. final concentration lipid concentrate from
GIBCO+2.5 g/L Wheat Peptone E1 from Organo Technie. Medi SFM 104:
Taub's+1.times. final concentration lipid concentrate from
GIBCO+2.5 g/L Wheat Peptone E1 from Organo Technie+0.01 .mu.g/mL
EGF (multiple sources). Medi SFM105: Taub's without Transferrin,
+1.times. final concentration lipid concentrate from GIBCO+2.5 g/L
Wheat Peptone E1 from Organo Technie+0.01 .mu.g/mL EGF+Ferric
ammonium citrate:Tropolone or Ferric ammonium sulfate:Tropolone at
a ratio of between 10 to 1 and 70 to 1.
Adaptation of MDCK-S cells into Serum-free MediV SFM media
formulations: A frozen vial of MDCK cell from ATCC was grown in 10%
FBS DMEM medium with 4.5 g/L glucose, 2.2 g/L NaHCO.sub.3 and 4 mM
L-glutamine for 5 passages (as described above) before passaging
into a MediV SFM media formulation (MediV SFM 101, MediV SFM 102 or
MediV SFM 103). Serum MDCK grown in a T-75 flask were recovered by
trypsinization. The spent growth medium was removed and cell
monolayer washed twice with DPBS (calcium and magnesium free) and
then DPBS was discarded. The appropriate amount of pre-warmed
trypsin-EDTA (3 mL/T-75) was added and the T-flask was incubated in
a 37.degree. C., 5% CO.sub.2 incubator for about 15 min. The flasks
were rapped against the palm of the hand several times to
completely detach the cells. Equal volume of lima bean trypsin
inhibitor was added to neutralize the trypsin and two samples were
taken to determine concentration of cells in the cell suspension.
1.75.times.10.sup.6 cells were then diluted into 35 mL of the
desired MediV SFM media formulation in a fresh T75 flask. The flask
was placed in an cell culture incubator maintained at 5% CO.sub.2,
37.+-.1.degree. C. The cells were either subcultured 3 days post
seeding or a complete medium exchange was performed on day 3
followed by subculturing on day 4 postseeding. Cells maybe adapted
to MediV SF104 and MediV SF105 using the same procedure described
above.
Subculturing of MediV SFM media Adapted MDCK cells: The spent
growth medium was removed and cell monolayer washed twice with DPBS
(calcium and magnesium free). The appropriate amount of pre-warmed
trypsin-EDTA (3 mL/T-75, 7.5 mL/T-225) was added and the T-flask
was incubated in a 37.degree. C., 5% CO.sub.2 incubator for about
15 min. The flasks were rapped against the palm of the hand several
times to completely detach the cells. The trypsin was then
inhibited by addition of equal volumes of lima bean trypsin
inhibitor (3 mL/T-75, 7.5 mL/T-225). The cell suspension was
homogenized by aspirating up and down with an appropriately sized
pipette. Two 0.5 mL samples of cell suspension were taken for cell
counting. The cell counts were repeated if the results of the two
counts were not within 15% of each other. After counting, the cells
were diluted to 0.05.times.10.sup.6 viable cells/mL in the
appropriate fresh prewarmed MediV SFM media formulation in fresh
flasks, for a total volume of 35 mL/T75 or 100 mL/T-225. The flasks
were then incubated in a 37.+-.1.degree. C., 5% CO.sub.2
environment. Cells were either subcultured to new T-flasks on day 3
(as described below) or a complete media exchange was performed and
the culture subcultured to new T-flasks on day 4 post seeding.
Note: MDCK-SF cells are always subcultured into the same MediV SFM
media formulation as they were adapted to.
Preparation of MediV SFM media Adapted MDCK cell PreMCB Banks: The
pre-master cell banks for the serum-free adapted MDCK cell lines
are prepared as described in example 1 above, except that the
2.times. freezing medium is the appropriate MediV SFM media
formulation+15% DMSO.
Characterization of MediV SFM media Adapted MDCK (MDCK-SF) cells:
Karyology, sterility and mycoplasma testing of the MDCK-SF preMCBs
are tested according to methodology described herein, e.g., in
Example 2 except that the appropriate MediV SFM media formulation
is used in place of serum containing complete media. Further, the
growth curve characteristics of MDCK-SF cells in T-75 flasks and
the replication of cold adapted influenza strains in MDCK-SF cells
can be examined as described in Example 2 except that the
appropriate MediV SFM media formulation is used in place of serum
containing complete media. In addition, tumorigenicity studies can
be performed on MDCK-SF cells after an additional number of
passages (e.g., preMCB+20 passages) by a commercial contractor
(e.g., BioReliance) as described in Example 2 above.
Results and Discussion
The cell karyology of MDCK-SF101 and MDCK-SF102 cells was tested at
passage 71/9 and of MDCK-SF103 at passage 87. The distributions of
chromosome number in 100 metaphases of MDCK-T, MDCK-SF101 and
MDCK-SF102 cells are shown in FIG. 14 and of MDCK-SF103 in FIG. 19.
It can be seen that the MDCK-T cells show a wider spread in
chromosome number (52 to 84) as compared to MDCK-SF111, MDCK-SF102
or MDCK-SF103 cells (70-82, 60-80, and 66-80 respectively). The
spread in chromosome number for the MDCK-SF101, MDCK-SF102 and
MDCK-SF103 cells is much closer to that seen for the
non-tumorigenic MDCK-S serum grown cells (70-84) indicating that
the MediV SF101, MediV SF102, and MediV SF103 media formulations
are better able to maintain the normal chromosomal number of MDCK
cells grown in these formulations.
A representative preliminary growth curve for MDCK-SF103 cells in
MediV SF103 medium is showed in FIG. 16. MDCK-SF103 cells had about
a one day lag phase. The cells were in the exponential phase of
growth until about day 4, when they entered into the stationary
phase. During the exponential phase (day 0 to day 4) they utilized
glucose and glutamine (FIGS. 17 and 18) while producing lactate and
ammonia. The glucose consumption/lactate production rate correlated
well with the cell growth curve (see FIGS. 16 and 17). The maximum
cell density of .about.17.times.10.sup.6 was achieved around day 4
post seeding. The cell density did not drop during the stationary
phase and remained fairly constant till day 7.
The glutamine consumption rate and ammonia production rate were
similar to the MDCK-SF103 cell growth and glucose/lactate profiles
(see FIG. 18). Ammonia production increased linearly up to day 7
while the glutamate concentration did not change appreciably during
the 7 day period.
MDCK-SF103 cells were tested for their ability to support the
replication of several reassortant influenza strains as described
in Example 7 below. The results shown in FIG. 20A indicate that
MDCK-SF103 cells were able to support the replication of each
influenza strain tested.
The MDCK-SF103 cells were put on nude mice for tumorigenicity test
for 3 months as described above. The test article was deemed to be
non-tumorigenic in the adult nude mouse model RioReliance Study
Number AB09EU.001000.BSV).
TABLE-US-00004 TABLE 4 Tumorigenicity and Karyology of MDCK cells
passed in different medias. Estimated TP.sub.50* Cells (no animals
Karyology (passage Tumori- with tumors/ Median number; number)
genicity total animals) comments MDCK-S ND ND 78; Few cells with
(P61/4) anomalous chromosome number (70 to 82) MDCK-S No neo- Not
estimable 78; Few cells with (P81/24) plasias. (>10.sup.7)
anomalous chromosome Fibrosar- (0/10) number (70 to 82) comas at
injection site MDCK-T ND ND 78; Large distribution (P63/4) of cells
with chromosome number of 52 to 82 MDCK-T Neopla- ~10.sup.7 78;
Large distribution (P88/29)) sias (6/10) of cells with chromosome
noted number of 52-82 MDCK- ND ND 78; Few cells with SF101
anomalous chromosome number (70 to 82) MDCK- ND ND 78; Few cells
with SF102 anomalous chromosome number (60 to 80) MDCK- No neo- Not
estimable 78; Few cells with SF103 plasias. (>10.sup.7)
anomalous chromosome Fibrosar- (0/10) number (66 to 80) comas at
injection site *TP.sub.50: Number of cells required to induce
tumors in 50% of animals ND: Not done
Example 5
Infection of Human Epithelial Cells in Culture
To evaluate the biochemical, biological, and structural
similarities following replication of the MDCK and egg produced
vaccines in cells of human origin, vaccines is passaged once in
relevant diploid human cells, such as normal human bronchial
epithelial cells (NHBE). This passage serves to mimic a single
infection event in the human airway and then enable comparison of
the progeny virus, the virus that is ultimately responsible for
eliciting an effective immune response. Studies of the vaccines'
hemagglutinin (binding and fusion) and neuraminidase activities are
measured on these materials as well as other biochemical and
structural studies including electron microscopy, infectious to
total particle ratios, and viral genome equivalents are evaluated.
Overall, these comparisons serve to demonstrate the comparability
of the cell-derived vaccine to the effective and safe egg produced
vaccine. Methods for testing for the presence of bacterial and
fungal contaminants are well known in the art and routinely
performed by commercial contractors (e.g., BioReliance.RTM.,
Rockville, Md.). A summary of analytical studies which may be
performed is summarized in Table 5.
TABLE-US-00005 TABLE 5 Preclinical Studies To Compare Cell And Egg
Produced Vaccines In vivo (ferrets) Attenuation/Replication Extent
of replication in upper airway Kinetics of replication in upper
airway Immunogenicity Cross-reactivity Kinetics Infectivity Dose
required for detectable replication Dose required for antibody
response In vitro* Virus binding Hemagglutination titer Binding of
different sialic acids Phyical properties Morphology by EM
Infectious: Total particles (genomes) Fusion activity pH optimum
temperature optimum Genomic sequence Neuraminidase activity
Example 6
Production, Testing and Characterization of a Master Cell Bank
To initiate the generation of a master cell bank (MCB) cells from
one or more of the preMCBs described above (see, Examples 2-4) are
biologically cloned through limiting dilution in order to ensure
that the production cells are derived from a unique genetic
constellation. Clones are then screened for various phenotypic
properties including doubling time and relative tumorigenicity, as
well as viral production. In an initial proof of concept
experiment, fifty-four MDCK clones were obtained in media
containing FCS. These clones were passaged and each was infected
with a low multiplicity of infection of ca A/New Calcdonia/20/99.
Several days after infection, the supernatant was removed and the
quantity of virus in the supernatant was measured by TCID.sub.50. A
minority of the clones produced relatively high titers of virus,
greater than was produced in the noncloned parental cells. Clones
with superior biological and physiological properties are used to
establish a Master Cell Bank (MCB).
The MCB is extensively tested to ensure that there is no evidence
of adventitious agents. For example, one or more of several PCR
and/or antibody-specific tests for available viral agents are
conducted, as shown in Table 6, below.
TABLE-US-00006 TABLE 6 Testing Regimen For a MCB General tests
Sterility Mycoplasma Adventitious agents in vitro (multiple cell
lines) Adventitious agents in vivo PERT Co-cultivation Karyology
Electron microscopy Tumorigenicity intact cells (TP.sub.50)
Oncogenicity of cellular DNA Oncogenicity of cellular lysate Bovine
viruses per 9CFR Porcine viruses per 9CFR PCR*/Ab specific AAV
Types 1 & 2 HCMV EBV HSV Hepatitis B, C & E HHV 6, 7 &
8 HIV 1 & 2 HPV HTLV I & II Polyoma (BK and JC viruses)
Circovirus Canine Parvovirus Canine distemper Adenovirus SV40
Example 7
Process and Formulation of Vaccine Material
Use of a highly scalable microcarrier technology, similar to that
used for the production of the currently licensed Polio vaccine, is
applicable to the production of influenza in MDCK cells. Spherical
beads made of dextran support excellent growth of MDCK cells and in
2 to 10 L bioreactors. Parental MDCK cells grown in SFMV 103 were
found to be capable of growing on Cytodex 1 microcarriers to a
density of 2.times.10.sup.6 nuclei per mL in batch mode in both
spinner flasks and MDCK cells have been grown to
>1.times.10.sup.6 cell/mL in bioreactors up to a 10 L scale
(data not shown). Initial pilot scale runs demonstrate that these
MDCK cells are capable of producing vaccine influenza strains to
high titer in a serum-free process and the titers were found to be
equivalent or greater than the productivity obtained using serum
grown cells in T-flasks. As shown in FIG. 20A, MDCK cells grown in
Cytodex beads in 250 mL spinner flasks produced high titers of
H1N1, H3N2 and B vaccine strains. For clinical manufacturing
influenza virus may be produced in MDCK cells at the 20 L or 150 L
scale, while commercial scale production may utilized 2,500 L
bioreactors. FIG. 20B outlines one process that may be used for
cell culture scale up to commercial production levels. The working
cell bank is first expanded sequentially from a T-75 flask to T-225
flasks to 1 liter spinner flasks to a 20 liter then 300 liter
bioreactors which are finally expanded to a 2500 liter bioreactor.
When the optimal cell density is obtained the culture in inoculated
with the master viral strain. The virus is then bulk harvested from
the culture supernatant.
The purification process for cell culture based influenza vaccines
is modeled on purification of egg-based influenza vaccines (see,
e.g., PCT Publication WO 05/014862 and PCT Patent Application
PCT/US05/035614 filed Oct. 4, 2005). The purification of viral
vaccine materials from cells may include any or all of the
following processes, homogenation, clarification centrifugation,
ultrafiltration, adsorption on barium sulfate and elution,
tangential flow filtration, density gradient ultracentrifugation,
chromatography, and sterialization filtration. Other purification
steps may also be included. For example, crude medium from infected
cultures can first be clarified by centrifugation at, e.g.,
1000-2000.times.g for a time sufficient to remove cell debris and
other large particulate matter, e.g., between 10 and 30 minutes.
Alternatively, the medium is filtered through a 0.8 .mu.m cellulose
acetate filter to remove intact cells and other large particulate
matter. Optionally, the clarified medium supernatant is then
centrifuged to pellet the influenza viruses, e.g., at
15,000.times.g, for approximately 3-5 hours. Following resuspension
of the virus pellet in an appropriate buffer, such as STE (0.01 M
Tris-HCl; 0.15 M NaCl; 0.0001 M EDTA) or phosphate buffered saline
(PBS) at pH 7.4, the virus may be concentrated by density gradient
centrifugation on sucrose (60%-12%) or potassium tartrate
(50%-10%). Either continuous or step gradients, e.g., a sucrose
gradient between 12% and 60% in four 12% steps, are suitable. The
gradients are centrifuged at a speed, and for a time, sufficient
for the viruses to concentrate into a visible band for recovery.
Alternatively, and for most large scale commercial applications,
virus is elutriated from density gradients using a zonal-centrifuge
rotor operating in continuous mode.
A feature which may included in the purification of viral vaccine
materials from cells is the use of Benzonase.RTM., a non-specific
endonuclease, early in the process. While MDCK cellular DNA does
not pose an oncogenic risk based on studies evaluating oncogenicity
of cellular DNA, Benzonase.RTM. treatment would virtually eliminate
any potential or hypothetical risk. In one purification process,
following Benzonase.RTM. treatment, the material is clarified by
direct flow filtration (DFF) which will also remove any residual
intact mammalian cells in the bulk material. The filtered bulk is
then concentrated by tangential flow filtration (TFF) prior to
further purification steps. Purification methods including affinity
chromatography as well as ion-exchange chromatography and/or
hydroxyapatite which, have worked well for other viral systems are
useful for cell culture based influenza vaccine production. The
highly purified viral material obtained by the process developed is
then utilized in the production of vaccine material. For example,
for use in a live attenuated vaccine production (e.g.,
FluMist.RTM.) the viral material may be subjected to a buffer
exchange by filtration into a final formulation followed by a
sterilization step. Buffers useful for such a formulation may
contain 200 mM sucrose and a phosphate or histidine buffer of pH
7.0-7.2 with the addition of other amino acid excipients such as
arginine. If necessary for stabilization protein hydrolysates such
as porcine gelatin may also be added. Ideally the vaccine material
is formulated to be stable for an extended storage time. One method
which may be utilized to extend storage time is spray drying, a
rapid drying process whereby the formulation liquid feed is spray
atomized into fine droplets under a stream of dry heated gas. The
evaporation of the fine droplets results in dry powders composed of
the dissolved solutes (see, e.g., US Patent Publication
2004/0042972). Spray drying offers the advantages of ease of
scalability and manufacturing cost as compared to conventional
freeze-drying processes. Alternatively, the vaccine material is
formulated to be stable as a refrigerator stable liquid formulation
using methods known in the art. For example, methods and
compositions for formulating a refrigerator stable attenuated
influenza vaccine are described in PCT Patent Application
PCT/US2005/035614 filed Oct. 4, 2005.
In-process characterization steps are incorporated into the
purification scheme to monitor the production. Characterization
steps which may be utilized include but are not limited to
Fluorescent Focus Assay (FFA, see, e.g., above) which uses a simple
antibody binding and fluorescent staining method to determine virus
infectivity. Total protein and DNA determination which may be
performed using numerous methods known to one of skill in the art
are used to determine the percent of the initial impurities
remaining. The specific activity of the preparation may be
determined by calculating the viral infectivity per quantity of
vaccine (e.g., infectivity/mg).
Example 8
Preclinical Animal Models
The ferret is a robust animal model used to evaluate the
attenuation and immunogenicity of attenuated influenza vaccines and
component vaccine strains. The performance of cell derived
influenza strains produced from the MCB are compared to the same
strains produced in eggs. Head to head comparison of these
materials in controlled studies enables a high level of assurance
of the comparability of these viral products.
In order to evaluate the ability of the two vaccines to infect or
achieve a "take" in the ferret, animals are lightly anesthetized
and inoculated intranasally with either the cell or egg produced
viral preparations. Nasal wash material is collected at several
time points following inoculation and the quantity of virus is
evaluated by one of several available methods in order to evaluate
the kinetics and extent of viral replication in the animals' upper
respiratory tract. Experiments are performed with a range of doses
and include multiple strains and different trivalent mixtures to
generalize the relative infectivity of cell culture grown strains
to egg produced strains. These same studies are also used to
evaluate the immunogenicity of the influenza strains, a property
that is inherently linked to the ability of the virus to initiate
infection. Animals are bled and nasal washes are harvested at
various points (weeks) post inoculation; these specimens are used
to assess the serum antibody and nasal IgA responses to infection.
The culmination of these data, infectivity, serum antibody and
mucosal antibody responses, will be used to compare and evaluate
the relative infectivity of the cell-produced vaccine to the egg
produced vaccine. The most likely outcome is predicted to be that
the cell and egg produced vaccine strains have similar infectivity
and immunogenicity. If the cell derived vaccine appeared to be more
infective or more immunogenic than the egg-derived product, further
studies evaluating the possibility of lower dosage are
performed.
A number of immunogenicity and replication studies are performed in
the ferret model to evaluate the cell culture-derived vaccines with
a single unit human dose. Infection with ca/ts/att strains
generally elicits strong and rapid antibody responses in ferrets.
In addition, individual ca/ts/att strains are routinely tested and
shown to express the attenuated (att) phenotype by replicating to
relatively high titers in the nasopharynx but to undetectable
levels in the lung of these animals. The impact of cell culture
growth on these biological traits is also assessed. However, it is
unlikely that any differences will be seen, since the att phenotype
is an integral part of the genetic composition of these strains.
The growth kinetics and crossreactivity of these strains is
evaluated following administration of a single human dose in these
animals. Live attenuated vaccines generated from egg derived
material elicit serum antibodies that cross-react with multiple
strains within a genetic lineage; and it is expected that a
cell-derived vaccine will have the same capability.
These comparability evaluations should provide significant insight
into potential biochemical and/or biophysical differences of the
primary virus product and demonstrate the impact of these
epigenetic differences on the performance of the ca/ts/att strains
measured by first passaging the virus in human cells or animal
studies. Based on the sequence information to date, there is no
expected impact on the ca/ts/att strains immunogenic performance
resulting from production on MDCK cells.
Ferrets are a well document animal model for influenza and are used
routinely to evaluate the attenuation phenotype and immunogenicity
of ca/ts/att strains. In general, 8-10 week old animals are used to
assess attenuation; typically study designs evaluate n=3-5 animals
per test or control group. Immunogenicity studies are evaluated in
animals from 8 weeks to 6 months of age and generally require n=3-5
animals per test article or control group. These numbers provide
sufficient information to obtain statistically valid or
observationally important comparisons between groups. During most
studies Influenza-like signs may be noticed, but are not likely.
Ferrets do not display signs of decrease in appetite or weight,
nasal or ocular discharge; observing signs of influenza-like
illness is a necessary part of the study and interventions such as
analgesics are not warranted. Other signs of discomfort, such as
open sores or significant weight loss, would result in appropriate
disposition of the animal following discussion with the attending
veterinarian.
While this invention has been disclosed with reference to specific
embodiments, it is apparent that other embodiments and variations
of this invention may be devised by others skilled in the art
without departing from the true spirit and scope of the invention.
The appended claims are intended to be construed to include all
such embodiments and equivalent variations. For example, all the
techniques and apparatus described above may be used in various
combinations. All publications, patents, patent applications, or
other documents cited in this application are incorporated by
reference in their entirety for all purposes to the same extent as
if each individual publication, patent, patent application, or
other document were individually indicated to be incorporated by
reference for all purposes.
* * * * *
References